CONSEQUENCE CALCULATIONS - Environment and … DPS_QRA Annex E... · CONSEQUENCE CALCULATIONS B.01a - GAS TANKER (RELEASE ON WATER) RELEASE Case description: B01a_TANK_G1_RELEASE

Project for a new LNG regasification facility to be located in the Marsaxlokk Bay – QRA PRELIMINARY REPORT

Ref: 02-901-188098-12141-Revision 2 Page E.1 of E.425

CONSEQUENCE CALCULATIONS B.01a - GAS TANKER (RELEASE ON WATER) RELEASE Case description: B01a_TANK_G1_RELEASE Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)Type of release Release through hole in vesselPipeline length (m) Pipeline diameter (mm) Pipeline roughness (mm) Hole diameter (m) 53Hole rounding Rounded edgesDischarge coefficient (-) 1Height difference between pipe entrance and exit (m) Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 90000Vessel type Vertical cylinderHeight cylinder (m) 40Filling degree (%) 90Expansion type Adiabaticn value Pressure inside vessel determination Use actual pressureInitial (absolute) pressure in vessel (bar) 1,0543Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 3,4181E07Initial (vapour) pressure in vessel (bar) 1,0543Time needed to empty vessel (s) 2,3858Massflowrate at end outflow (kg/s) 0Total mass released (kg) 3,0878E07Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -163,2VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 3,1716E06Vapour mass in vessel at end outflow (kg) 1,3126E05Height of liquid at end outflow (m) 3,3164Fillingdegree at end outflow (%) 8,2911Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -163,2Maximum mass flow rate (kg/s) 2,5049E07Representative release rate (kg/s) 2,2856E07Representative outflow duration (s) 1Representative temperature (°C) -161,13Representative pressure at exit (bar) 2,3393Representative vapour mass fraction (%) 0 Other information Main program Effects 8.1.8.6673



Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010

Effects report created by ESLR2RH1F\andrea_silvasantos at 25/07/2013 16:20:35

VAPORISATION Case description: B01a_TANK_G1_FLASH (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE) Model: Liquefied Gas Spray Release version: 5.05 (25/07/2013) Reference: Yellow Book CPR14E, Page: 2.105 / 2.112, Section: 2.5.3.7 [Finite duration spray releases] / 2.5.3.8 [Instantaneous release of pressurised liquefied vapours] Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Mass flow rate of the source (kg/s) 2,2856E07Exit temperature (°C) -161,13Exit pressure (bar) 2,3393Exit vapour mass fraction (%) 0Hole diameter (mm) 53000Height leak above ground level (m) 1Ambient temperature (°C) 19Ambient relative humidity (%) 75

Results AFTER FLASHING AND RAINOUT: liquid mass fraction (%) 99,798Nett mass flow to air (jet) (kg/s) 2,2856E07Temperature jet/cloud (°C) -161,49Diameter jet/cloud (m) 52,017Nett mass flow rained out (kg/s) 0Temperature of the pool (°C) -161,49Density of the airborn mass (kg/m3) 284,73 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


POOL EVAPORATION Case description: B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE) Model: Pool evaporation version: 5.16 (25/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE) compared to: B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE) compared to: B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE) Parameters

Inputs B01a_TANK_G1_EVAP_D3 (linked to Liquefied

B01a_TANK_G1_EVAP_D9 (linked to Liquefied

B01a_TANK_G1_EVAP_E5 (linked to Liquefied

B01a_TANK_G1_EVAP_F2 (linked to Liquefied



Gas Bottom Discharge (TPDIS model) -

B01a_TANK_G1_RELEASE)







Chemical name (DIPPR)

METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Use which representative step

First 20% average (flammable)




Evaporation from land or water

Land Land Land Land

Type of release

Instantaneous Instantaneous Instantaneous Instantaneous

Mass flow rate of the source (kg/s)

2,2856E07 2,2856E07 2,2856E07 2,2856E07

Duration of the release (s)

1 1 1 1

Total mass released (kg)

3,0878E07 3,0878E07 3,0878E07 3,0878E07

Height pool at t=0

Calculate/Default Calculate/Default Calculate/Default Calculate/Default

Value pool height at t=0 (m)

Type of pool growth on Land

Spreading in bunds Spreading in bunds Spreading in bunds Spreading in bunds

Type of pool growth on Water

Temperature of the pool (°C)

19 19 19 19

Maximum pool surface area (m2)

2206 2206 2206 2206

Temperature of the subsoil (°C)

19 19 19 19

Temperature of the water (°C)

Max temperature difference between pool and water (K)

Wind speed at 10 m height (m/s)

3 9 5 2

Ambient temperature (°C)

19 19 19 19

Ambient relative humidity (%)

75 75 75 75

Solar User defined User defined User defined User defined



radiation flux Solar heat radiation flux (W/m2)

100 100 100 100

Cloud cover (%)

Date: day number

Date: month number

Date: year number

Latitude of the location (deg)

Type of subsoil

Heavy concrete Heavy concrete Heavy concrete Heavy concrete

Subsoil roughness description

flat sandy soil, concrete, tiles, plant-yard




Maximum evaluation time for evaporation (s)

1800 1800 1800 1800

Results

B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge

(TPDIS model) -B01a_TANK_G1_RELE

ASE)

B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge


ASE)

B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge


ASE)

B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge


ASE)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1

Time pool spreading ends (s)

Time until pool has totally evaporated (s)

Purple book representative evaporation rate (kg/s)

118,62 116,07 99,648 133,75

Purple book representative evaporation duration (s)

757,41 1565,7 1219,4 561,47

Representative temperature (°C)

-161,49 -161,49 -161,49 -161,49

Representative pool diameter (m)

52,998 52,998 52,998 52,998

Density after mixing with

1,5452 1,3829 1,4419 1,6208



air (kg/m3) Total evaporated mass (kg)

89846 1,8173E05 1,2151E05 75096

... duration evaporation time (s)

1799,5 1799,5 1799,5 1799,5

Corresponding representative pool surface area (m2)

2206 2206 2206 2206

Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


ATMOSPHERIC DISPERSION Case description: B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE)) compared to: B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE)) compared to: B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE)) Parameters

Inputs

B01a_TANK_G1_DISPERSION D3 (linked to

Pool evaporation -TANK_G1_EVAP_D3

(linked to Liquefied GasBottom Discharge

(TPDIS model) -TANK_G1_RELEASE))



(linked to Liquefied Gas Bottom Discharge


B01a_TANK_G1_DISPERSION E5 (linked to Pool

evaporation -TANK_G1_EVAP_E5



B01a_TANK_G1_DISPERSION F2 (linked to Pool

evaporation -TANK_G1_EVAP_F2





Type of release

Evaporating pool release Evaporating pool release Evaporating pool release Evaporating pool release


3,0878E07 3,0878E07 3,0878E07 3,0878E07


118,62 116,07 99,648 133,75


757,41 1565,7 1219,4 561,47

Initial liquid mass



fraction (%) Fixed pool surface (m2)

2206 2206 2206 2206

Diameter of expanded jet (m)

Temperature after release (°C)

-161,49 -161,49 -161,49 -161,49

X-coordinate of release (m)

0 0 0 0

Y-coordinate of release (m)

0 0 0 0

Z-coordinate (height) of release (m)


19 19 19 19

Meteorological data

Pasquill Pasquill Pasquill Pasquill

Pasquill stability class

D (Neutral) D (Neutral) E (Stable) F (Very Stable)


3 9 5 2

Inverse Monin-Obukhov length (1/L) (1/m)

Predefined wind direction

N N N N

Wind comes from (North = 0 degrees) (deg)

0 0 0 0


75 75 75 75

Roughness length description

High crops; scattered large objects, 15 < x/h <

20.


20.


20.


20.Time t after start release (s)

1800 1800 1800 1800

Concentration averaging

20 20 20 20



time (s) Resolution of the time consuming graphs

Low Low Low Low

Results









B01a_TANK_G1_DISPERSION E5 (linked to Pool




B01a_TANK_G1_DISPERSION F2 (linked to Pool




Explosive mass at time t (kg)

0 0 0 0

Height to LEL at time t (m)

0 0 0 0

Length of cloud (between LEL) at time t (m)

0 0 0 0

Width of cloud (between LEL) at time t (m)

0 0 0 0

Offset between release location and LEL at time t (m)

0 0 0 0

Maximum explosive mass (kg)

5155 0 2985,6 3,2752E05

...at time tmem (s)

100 2000 1200 700

Start time where 95% of maximum of explosive mass is reached (s)

90,355 0 95 693,35

Time where explosive mass starts decreasing below 95% of max (s)

757,41 2000 1219,4 731,73

Length of cloud (between LEL) at time tmem (m)

275,68 0 269,9 1841

Width of 73,367 0 71,114 1974,9



cloud (between LEL) at time tmem (m) Offset between release location and LEL at time tmem (m)

-30,456 0 -29,729 71,699

Maximum area of explosive cloud (m2)

15595 0 14130 6,7748E05

...at time tmac (s)

757,41 1565,7 1219,4 700

Explosive mass at time tmac (kg)

5155 0 2985,6 3,2752E05

Length of cloud (between LEL) at time tmac (m)

275,9 0 269,9 1841

Width of cloud (between LEL) at time tmac (m)

73,352 0 71,114 1974,9

Offset between release location and LEL at time tmac (m)

-30,456 0 -29,729 71,699

Offset between release centre and cloud centre at time tmac (m)

107,49 0 105,22 992,22

Inverse Monin-Obukhov length (1/L) used (1/m)

0 0 0,012352 0,048833





EXPLOSION Case description: B01a_TANK_G1_D3_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01a_TANK_G1_D9_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: TANK_G1_E5_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE))) compared to: TANK_G1_F2_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G1_RELEASE))) Parameters

Inputs

TANK_G1_D3_UVCE (linked to Dense Gas Dispersion: Explosive

mass -B01a_TANK_G1_DISPE

RSION D3 (linked to Pool evaporation -

TANK_G1_EVAP_D3 (linked to Liquefied Gas

Bottom Discharge (TPDIS model) -

TANK_G1_RELEASE)))


mass - B01a_TANK_G1_DISPE




TANK_G1_RELEASE)))

TANK_G1_E5_UVCE (linked to Dense Gas Dispersion: Explosive

mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool



(TPDIS model) -TANK_G1_RELEASE)))

TANK_G1_F2_UVCE (linked to Dense Gas Dispersion: Explosive

mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool






Ambient pressure (bar)

1,0151 1,0151 1,0151 1,0151

Total mass in explosive range (kg)

5155 0 2985,6 3,2752E05

Fraction of flammable cloud confined (%)

8 8 8 8

Curve number

5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration)

Distance from release (Xd) (m)

50 50 50 50

Offset between release point and cloud centre (m)

107,49 0 105,22 992,22

Threshold overpressure (mbar)

100 100 100 100

X-coordinate of release

0 0 0 0



(m) Y-coordinate of release (m)

0 0 0 0


N N N N


0 0 0 0

Results


mass -B01a_TANK_G1_DISPE




TANK_G1_RELEASE)))


mass - B01a_TANK_G1_DISPE




TANK_G1_RELEASE)))


mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool





mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool




Confined mass in explosive range (kg)

412,4 0 238,85 26201

Total combustion energy (MJ)

20633 -1E94 11950 1,3109E06

Peak overpressure at Xd (mbar)

143,9 -1E98 119,14 206,07

Peak dynamic pressure at Xd (mbar)

20,924 -1E98 13,575 68,044

Pressure impulse at Xd (Pa*s)

843,2 -1E100 587,9 5106,8

Positive phase duration at Xd (ms)

117,2 -1E103 98,69 495,65

Dist. from center mass of cloud at threshold overpressure (m)

71,745 -1E100 59,803 286,28

Blast-wave shape at Xd

Pressure wave *** NOT INITIALIZED Pressure wave Pressure wave

Damage Minor damage (Zone D: No damage or very Minor damage (Zone D: Moderate damage



(general description) at Xd

3.5 - 17 kPa). minor damage 3.5 - 17 kPa). (Zone C: 17 - 35 kPa).

Damage to brick houses at Xd

Not habitable without major repair works.

Partial roof failures, 25% of all brick walls have

failed, serious damage to the remaining carrying elements. Damage to

windowframes and doors (7-15 kPa).

No damage or very minor damage









Damage to typical American-style houses at Xd

Minor damage. Comparable to a damage

due to a storm; wooden walls fail, breakage of windows (7-10 kPa).




Moderate to minor damage. Deformed

walls and doors; failure of joints. Doors and

window frames have failed. Wall covering has fallen down (15

kPa).

Damage to structures (empirical) at Xd

Minor damage to steel frames (8-10 kPa).

Connections between steel or aluminium

ondulated plates have failed 7-14 kPa). The roof

of a storage tank has collapsed (7 kPa).






Collapse of steel frames and

displacement of foundation (20 kPa). Industrial steel self-

framing structure collapsed (20-30 kPa). Cracking in empty oil-

storage tanks (20-30 kPa). Slight

deformation of a pipe-bridge (20-30 kPa).

Large trees have fallen down (20-40 kPa). Walls

made of concrete blocks have collapsed (15-20). Minor damage

to steel frames (8-10 kPa). Connections

between steel or aluminium ondulated

plates have failed 7-14 kPa). The roof of a

storage tank has collapsed (7 kPa).



POOL FIRE Case description: B01a_TANK_G1_PFIRE D3 Model: Pool fire version: 5.11 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4



compared to: B01a_TANK_G1_PFIRE D9 compared to: B01a_TANK_G1_PFIRE E5 compared to: B01a_TANK_G1_PFIRE F2 Parameters

Inputs B01a_TANK_G1_PFIRE

D3B01a_TANK_G1_PFIRE

D9 B01a_TANK_G1_PFIRE

E5B01a_TANK_G1_PFIRE

F2Chemical name (DIPPR)


Pool size determination

Confined Confined Confined Confined


3,0878E07 3,0878E07 3,0878E07 3,0878E07



Pool surface poolfire (m2)

2206 2206 2206 2206

Height of the observer position above ground level (m)

0 0 0 0

Height of the confined pool above ground level (m)

0 0 0 0

Hole diameter (mm)

Discharge coefficient (-)

Initial height of the liquid above release point (m)

Cross-sectional area of the tank (m2)

Pool thickness (mm)


19 19 19 19

Pool burning rate


Value of pool burning rate (kg/m2*s)

Fraction combustion heat radiated (%)

35 35 35 35

Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of soot fraction (-)


3 9 5 2


19 19 19 19




75 75 75 75

Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03

Distance from the centre of the pool (m)

1000 1000 1000 1000

Exposure duration to heat radiation (s)

20 20 20 20

Take protective effects of clothing into account

No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Calculate all contours for

Physical effects Physical effects Physical effects Physical effects

Heat radiation level (lowest) for first contour plot (kW/m2)

6,8 6,8 6,8 6,8

Heat radiation level for second contour plot (kW/m2)

9,23 9,23 9,23 9,23

Heat radiation level (highest) for third contour plot (kW/m2)

13,4 13,4 13,4 13,4

Percentage of mortality for contour calculations (%)

Results B01a_TANK_G1_PFIRE

D3B01a_TANK_G1_PFIRE

D9 B01a_TANK_G1_PFIRE

E5B01a_TANK_G1_PFIRE

F2Max Diameter of the Pool Fire (m)

52,998 52,998 52,998 52,998

Heat radiation at X (kW/m2)

0,024267 0,016833 0,020802 0,026237

Heat radiation first contour at (m)

102,57 99,201 102,58 99,747

Heat radiation 91,122 90,931 92,641 87,758



second contour at (m) Heat radiation third contour at (m)

77,746 81,665 81,169 73,724

Combustion rate (kg/s)

172,07 172,07 172,07 172,07

Duration of the pool fire (s)

1,7945E05 1,7945E05 1,7945E05 1,7945E05

Heat emission from fire surface (kW/m2)

67,437 77,051 71,399 67,437

Flame tilt (deg)

40,884 56,324 48,526 34,492

View factor (%)

0,078803 0,046687 0,063139 0,085203

Atmospheric transmissivity (%)

45,663 46,794 46,143 45,663

Flame temperature (°C)

772,73 807,96 787,68 772,73

Height of the Flame (m)

57,115 46,034 52,082 57,115

Calculated pool surface area (m2)

2206 2206 2206 2206

Weight ratio of HCL/chemical (%)

0 0 0 0

Weight ratio of NO2/chemical (%)

0 0 0 0

Weight ratio of SO2/chemical (%)

0 0 0 0

Weight ratio of CO2/chemical (%)

274,4 274,4 274,4 274,4

Weight ratio of H2O/chemical (%)

224,69 224,69 224,69 224,69





B.01b - GAS TANKER (RELEASE ON WATER) RELEASE Case description: TANK_G2_RELEASE Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)Type of release Release through hole in vesselPipeline length (m) Pipeline diameter (mm) Pipeline roughness (mm) Hole diameter (mm) 1000Hole rounding Rounded edgesDischarge coefficient (-) 1Height difference between pipe entrance and exit (m) Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 90000Vessel type Vertical cylinderHeight cylinder (m) 40Filling degree (%) 90Expansion type Adiabaticn value Pressure inside vessel determination Use vapour pressureInitial (absolute) pressure in vessel (bar) 1,0543Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 3,4181E07Initial (vapour) pressure in vessel (bar) 1,0543Time needed to empty vessel (s) 6661,7Massflowrate at end outflow (kg/s) 0Total mass released (kg) 3,0818E07Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -163,24VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 3,2321E06Vapour mass in vessel at end outflow (kg) 1,3066E05Height of liquid at end outflow (m) 3,3792Fillingdegree at end outflow (%) 8,4481Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -163,24Maximum mass flow rate (kg/s) 8917,5Representative release rate (kg/s) 8363,6Representative outflow duration (s) 1800Representative temperature (°C) -161,06Representative pressure at exit (bar) 2,4169Representative vapour mass fraction (%) 0 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




VAPORISATION Case description: B01b_TANK_G2_FLASH (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE) Model: Liquefied Gas Spray Release version: 5.05 (25/07/2013) Reference: Yellow Book CPR14E, Page: 2.105 / 2.112, Section: 2.5.3.7 [Finite duration spray releases] / 2.5.3.8 [Instantaneous release of pressurised liquefied vapours] Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Mass flow rate of the source (kg/s) 8363,6Exit temperature (°C) -161,06Exit pressure (bar) 2,4169Exit vapour mass fraction (%) 0Hole diameter (mm) 1000Height leak above ground level (m) 1Ambient temperature (°C) 19Ambient relative humidity (%) 75

Results AFTER FLASHING AND RAINOUT: liquid mass fraction (%) 99,75Nett mass flow to air (jet) (kg/s) 8363,6Temperature jet/cloud (°C) -161,49Diameter jet/cloud (m) 1,0178Nett mass flow rained out (kg/s) 0Temperature of the pool (°C) -161,49Density of the airborn mass (kg/m3) 264,08 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


POOL EVAPORATION Case description: B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Model: Pool evaporation version: 5.16 (25/07/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) compared to: B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) compared to: B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Parameters

Inputs

B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge

(TPDIS model) - B01_b_TANK_G2_RELE

ASE)


(TPDIS model) -B01_b_TANK_G2_RELE

ASE)

B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge


ASE)

B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge


ASE)Chemical name (DIPPR)










Land Land Land Land

Type of release

Continuous Continuous Continuous Continuous


8363,6 8363,6 8363,6 8363,6


1800 1800 1800 1800


3,0818E07 3,0818E07 3,0818E07 3,0818E07

Height pool at t=0






19 19 19 19


2206 2206 2206 2206


19 19 19 19




3 9 5 2


19 19 19 19


75 75 75 75

Solar radiation flux

User defined User defined User defined User defined

Solar heat radiation flux (W/m2)

100 100 100 100

Cloud cover



(%) Date: day number

Date: month number

Date: year number


Type of subsoil

Heavy concrete Heavy concrete Heavy concrete Heavy concrete







1800 1800 1800 1800

Results



ASE)



ASE)

B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge


ASE)

B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge


ASE)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1


18 18 18 18



88,095 103,06 81,915 94,007


977,36 1674,9 1424,1 761,46


-161,49 -161,49 -161,49 -161,49


30,775 33,756 28,917 32,451

Density after mixing with air (kg/m3)

1,5817 1,4272 1,5033 1,6388

Total evaporated

86100 1,7262E05 1,1666E05 71583



mass (kg) ... duration evaporation time (s)

1799,5 1799,5 1799,5 1799,5


743,84 894,91 656,72 827,07



ATMOSPHERIC DISPERSION Case description: B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/07/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE)) compared to: B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE)) compared to: B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE)) Parameters

Inputs

B01b_TANK_G2_DISPERSION D3 (linked to








B01b_TANK_G2_DISPERSION E5 (linked to Pool




B01b_TANK_G2_DISPERSION F2 (linked to Pool






Type of release



3,0818E07 3,0818E07 3,0818E07 3,0818E07


88,095 103,06 81,915 94,007


977,36 1674,9 1424,1 761,46

Initial liquid mass fraction (%)

Fixed pool surface

743,84 894,91 656,72 827,07



(m2) Diameter of expanded jet (m)


-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75



20.


20.


20.


20.Time t after start release (s)

1800 1800 1800 1800

Concentration averaging time (s)

20 20 20 20

Resolution of the time

Low Low Low Low



consuming graphs

Results









B01b_TANK_G2_DISPERSION E5 (linked to Pool




B01b_TANK_G2_DISPERSION F2 (linked to Pool





0 72,098 0 0


0 4 0 0


0 18,719 0 0


0 40,156 0 0


0 -18,587 0 0


5250,3 698,1 2295,8 8,3549E05

...at time tmem (s)

800 500 1400 800


97,97 95 95 794,96


977,36 1674,9 1424,1 805


322,09 122,76 113,38 2306,5

Width of cloud (between LEL) at

49,314 42,957 46,598 1582,6



time tmem (m) Offset between release location and LEL at time tmem (m)

-18,379 -18,587 -17,229 -23,107


11264 3958,2 4759,4 1,3723E06

...at time tmac (s)

977,36 1674,9 1424,1 800


5250,3 698,1 2295,8 8,3549E05


322,09 18,719 113,38 2306,5


49,314 40,156 46,598 1582,6


-18,379 -18,587 -17,229 -23,107


142,67 -9,2275 39,459 1130,1


0 0 0,012352 0,048833



EXPLOSION



Case description: TANK_G2_D3_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: TANK_G2_D9_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE))) compared to: TANK_G2_E5_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE))) compared to: TANK_G2_F2_UVCE (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - TANK_G2_RELEASE))) Parameters

Inputs


mass -B01b_TANK_G2_DISPE




TANK_G2_RELEASE)))


mass - B01b_TANK_G2_DISPE




TANK_G2_RELEASE)))


mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool





mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool







1,0151 1,0151 1,0151 1,0151


5250,3 698,1 2295,8 8,3549E05


8 8 8 8

Curve number



50 50 50 50


142,67 -9,2275 39,459 1130,1


300 300 300 300


0 0 0 0




0 0 0 0


N N N N


0 0 0 0

Results


mass -B01b_TANK_G2_DISPE




TANK_G2_RELEASE)))


mass - B01b_TANK_G2_DISPE




TANK_G2_RELEASE)))


mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool





mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool





420,02 55,848 183,66 66839


21014 2794,1 9188,8 3,344E06


144,77 74,014 109,28 206,07


21,174 4,3341 11,055 68,044


853,35 229,21 495,99 6977,8


117,89 61,936 90,777 677,24


-1E100 -1E100 -1E100 -1E100


Pressure wave Pressure wave Pressure wave Pressure wave

Damage (general

Minor damage (Zone D: 3.5 - 17 kPa).



Moderate damage (Zone C: 17 - 35 kPa).



description) at Xd






Habitable after relatively easy repairs.

Minor structural damage (3 kPa).

















kPa).







ondulated plates have failed 7-14 kPa). The

roof of a storage tank has collapsed (7 kPa).










Large trees have fallen down (20-40 kPa). Walls

made of concrete blocks have collapsed (15-20). Minor damage







POOL FIRE Case description: B01b_TANK_G2_PFIRE D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Model: Pool fire version: 5.11 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B01b_TANK_G2_PFIRE D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)



compared to: B01b_TANK_G2_PFIRE E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) compared to: B01b_TANK_G2_PFIRE F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Parameters

Inputs

B01b_TANK_G2_PFIRE D3 (linked to Liquefied Gas Bottom Discharge


ASE)



ASE)

B01b_TANK_G2_PFIRE E5 (linked to Liquefied Gas Bottom Discharge


ASE)

B01b_TANK_G2_PFIRE F2 (linked to Liquefied Gas Bottom Discharge


ASE)Chemical name (DIPPR)





3,0818E07 3,0818E07 3,0818E07 3,0818E07


8363,6 8363,6 8363,6 8363,6


1800 1800 1800 1800


10000 10000 10000 10000


0 0 0 0


0 0 0 0

Hole diameter (mm)

1000 1000 1000 1000


1 1 1 1



Pool thickness (mm)




19 19 19 19

Pool burning rate




35 35 35 35

Soot Fraction


Value of soot fraction (-)


3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


20 20 20 20


No No No No


0 0 0 0


0 0 0 0


N N N N




0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4


Results



ASE)



ASE)

B01b_TANK_G2_PFIRE E5 (linked to Liquefied Gas Bottom Discharge


ASE)

B01b_TANK_G2_PFIRE F2 (linked to Liquefied Gas Bottom Discharge


ASE)Max Diameter of the Pool Fire (m)

112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194

Heat radiation first contourat (m)

198,96 193,87 200,39 195,03

Heat radiation second contour at (m)

177,63 177,35 181,02 172,64

Heat radiation third contour at (m)

153,44 159,19 159,19 147,33

Combustion rate

780 780 780 780



(kg/s) Duration of the pool fire (s)

39511 39511 39511 39511


78,846 87,066 80,77 78,846

Flame tilt (deg)

37,614 53,697 45,489 31,201

View factor (%)

0,30773 0,19824 0,26527 0,32729


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69





B.02a – GAS TANKER TO FSU UNLOADING ARM - LNG (RELEASE ON WATER) POOL EVAPORATION Case description: B02A_HARDARM_L1_L_EVAPORATION D3 Model: Pool evaporation version: 5.16 (25/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B02A_HARDARM_L1_L_EVAPORATION D9 compared to: B02A_HARDARM_L1_L_EVAPORATION E5 compared to: HB02A_ARDARM_L1_L_EVAPORATION F2 Parameters

Inputs B02A_HARDARM_L1_L_

EVAPORATION D3B02A_HARDARM_L1_L_

EVAPORATION D9 B02A_HARDARM_L1_L_

EVAPORATION E5HB02A_ARDARM_L1_L_

EVAPORATION F2Chemical name (DIPPR)








Water Water Water Water

Type of release



1407 1407 1407 1407


120 120 120 120


Height pool at t=0




Confined water surface Confined water surface Confined water surface Confined water surface


19 19 19 19


10000 10000 10000 10000





19 19 19 19


500 500 500 500


3 9 5 2


19 19 19 19


75 75 75 75




100 100 100 100

Cloud cover (%)

Date: day number

Date: month number

Date: year number


Type of subsoil


Maximum evaluatio

1800 1800 1800 1800



n time for evaporation (s)

Results

B02A_HARDARM_L1_L_EVAPORATION D3

B02A_HARDARM_L1_L_EVAPORATION D9

B02A_HARDARM_L1_L_EVAPORATION E5

HB02A_ARDARM_L1_L_EVAPORATION F2

Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1


54,5 54,5 54,5 54,5


250,5 250,5 250,5 250,5


1022,1 1022,1 1022,1 1022,1


165,32 165,32 165,32 165,32


-161,49 -161,49 -161,49 -161,49


112,84 112,84 112,84 112,84


1,7168 1,5894 1,6659 1,7468

Total evaporated mass (kg)

1,6897E05 1,6897E05 1,6897E05 1,6897E05


250,5 250,5 250,5 250,5

Corresponding represen

10000 10000 10000 10000



tative pool surface area (m2) Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


ATMOSPHERIC DISPERSION Case description: B02A_HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B02A_HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION D9) compared to: B02A_HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION E5) compared to: B02A_HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HB02A_ARDARM_L1_L_EVAPORATION F2) Parameters

Inputs

B02A_HARDARM_L1_L_DISPERSION D3 (linked

to Pool evaporation -B02A_HARDARM_L1_L_

EVAPORATION D3)



EVAPORATION D9)

B02A_HARDARM_L1_L_DISPERSION E5 (linked


EVAPORATION E5)

B02A_HARDARM_L1_L_DISPERSION F2 (linked

to Pool evaporation -HB02A_ARDARM_L1_L_

EVAPORATION F2)Chemical name (DIPPR)


Type of release




1022,1 1022,1 1022,1 1022,1


165,32 165,32 165,32 165,32


Fixed pool surface (m2)

10000 10000 10000 10000





-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75

Roughness length descripti

Cultivated land Cultivated land Cultivated land Cultivated land



on Time t after start release (s)

120 120 120 120


20 20 20 20

Resolution of the time consuming graphs

Low Low Low Low

Results



EVAPORATION D3)



EVAPORATION D9)



EVAPORATION E5)



EVAPORATION F2)Explosive mass at time t (kg)

89932 20467 54341 94021


41,2 14,8 46,9 10,5


332 451,86 262,22 427,26


178,32 146,06 181,66 292,22


-67,623 -63,147 -67,576 -127,38


1,1043E05 20467 94059 1,3065E05

...at time tmem (s)

175 150 175 175

Start time where 95% of maximum of

143,95 44,841 172,04 -1E100



explosive mass is reached (s) Time where explosive mass starts decreasing below 95% of max (s)

180,54 165,32 179,2 165,32


522,64 451,86 958,87 526,18

Width of cloud (between LEL) at time tmem (m)

160,43 146,06 320,41 339,57

Offset between release location and LEL at time tmem (m)

1,121 -63,147 -40,879 -119,73


56523 49218 1,0773E05 1,4939E05

...at time tmac (s)

175 165,32 225 175


1,1043E05 20467 27525 1,3065E05


522,64 451,86 383,05 526,18


160,43 146,06 373,76 339,57

Offset between

1,121 -63,147 758,01 -119,73



release location and LEL at time tmac (m) Offset between release centre and cloud centre at time tmac (m)

262,44 162,78 949,54 143,36


0 0 0,011686 0,04733



EXPLOSION Case description: B02A_HARDARM_L1_L_UVCE D3 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02A_HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B02A_HARDARM_L1_L_UVCE D9 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02A_HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION D9)) compared to: B02A_HARDARM_L1_L_UVCE E5 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02A_HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - B02A_HARDARM_L1_L_EVAPORATION E5)) compared to: B02A_HARDARM_L1_L_UVCE F2 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02A_HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HB02A_ARDARM_L1_L_EVAPORATION F2)) Parameters

Inputs

B02A_HARDARM_L1_L_UVCE D3 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02A_HARDARM_L1_L_DISPERSION D3 (linked


EVAPORATION D3))


Explosive mass -B02A_HARDARM_L1_L_DISPERSION D9 (linked


EVAPORATION D9))

B02A_HARDARM_L1_L_UVCE E5 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02A_HARDARM_L1_L_DISPERSION E5 (linked


EVAPORATION E5))

B02A_HARDARM_L1_L_UVCE F2 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02A_HARDARM_L1_L_DISPERSION F2 (linked


EVAPORATION F2))Chemical name (DIPPR)





1,0151 1,0151 1,0151 1,0151


1,1043E05 20467 27525 1,3065E05


8 8 8 8

Curve number



100 100 100 100


262,44 162,78 949,54 143,36


100 100 100 100


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results


Explosive mass -


Explosive mass -

B02A_HARDARM_L1_L_UVCE E5 LC1 (linked to Dense Gas Dispersion:

Explosive mass -

B02A_HARDARM_L1_L_UVCE F2 LC1 (linked to Dense Gas Dispersion:

Explosive mass -





EVAPORATION D3))



EVAPORATION D9))



EVAPORATION E5))



EVAPORATION F2))Confined mass in explosive range (kg)

8834,6 1637,3 2202 10452


4,4201E05 81918 1,1017E05 5,2294E05


193,85 113,15 125 199,29


44,49 12,063 15,101 50,575


3138,1 1063,5 1289,8 3439,8


323,77 187,97 206,36 345,21


199,26 113,6 125,4 210,74



Damage (general description) at Xd






Not habitable without major repair works. Partial

roof failures, 25% of all brick walls have failed, serious damage to the









remaining carrying elements. Damage to









Moderate to minor damage. Deformed walls

and doors; failure of joints. Doors and window frames have failed. Wall

covering has fallen down (15 kPa).

Minor damage. Comparable to a

damage due to a storm; wooden walls fail,

breakage of windows (7-10 kPa).





and doors; failure ofjoints. Doors and window frames have failed. Wall



Walls made of concrete blocks have collapsed

(15-20). Minor damage to steel frames (8-10 kPa).













(15-20). Minor damage to steel frames (8-10 kPa).






POOL FIRE Case description: B02A_HARDARM_L1_L_PFIRE D3 Model: Pool fire version: 5.11 (27/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B02A_HARDARM_L1_L_PFIRE D9 compared to: B02A_HARDARM_L1_L_PFIRE E5 compared to: B02A_HARDARM_L1_L_PFIRE F2 Parameters

Inputs B02A_HARDARM_L1_L

_PFIRE D3B02A_HARDARM_L1_L


_PFIRE E5B02A_HARDARM_L1_L

_PFIRE F2Chemical name (DIPPR)



Unconfined fixed feed Unconfined fixed feed Unconfined fixed feed Unconfined fixed feed



1407 1407 1407 1407


120 120 120 120

Pool surface poolfire



(m2) Height of the observer position above ground level (m)

0 0 0 0


Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35

Soot Fraction




3 9 5 2


19 19 19 19

Ambient 75 75 75 75



relative humidity (%) Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23

Heat radiation level (highest)

13,4 13,4 13,4 13,4



for third contour plot (kW/m2) Percentage of mortality for contour calculations (%)

Results B02A_HARDARM_L1_L



_PFIRE E5B02A_HARDARM_L1_L

_PFIRE F2Max Diameter of the Pool Fire (m)

115,17 115,17 115,17 115,17


0,11963 0,086781 0,10622 0,12717


202,57 197,46 204,02 198,57


180,87 180,56 184,31 175,8


156,24 162,09 162,11 150,11


812,54 812,54 812,54 812,54


207,79 207,79 207,79 207,79


79,178 87,351 81,038 79,178

Flame tilt (deg)

37,525 53,623 45,405 31,113

View factor (%)

0,31943 0,20629 0,27595 0,33956


47,299 48,16 47,501 47,299


815,31 842,23 821,61 815,31


95,698 81,439 92,138 95,698

Calculated pool surface

10417 10417 10417 10417



area (m2) Weight ratio of HCL/chemical (%)

0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69





B.02b– GAS TANKER TO FSU UNLOADING ARM - LNG (RELEASE ON WATER) POOL EVAPORATION Case description: B02B_HARDARM_L2_L_EVAPORATION D3 Model: Pool evaporation version: 5.16 (25/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B02B_HARDARM_L2_L_EVAPORATION D9 compared to: B02B_HARDARM_L2_L_EVAPORATION E5 compared to: B02B_HARDARM_L2_L_EVAPORATION F2 Parameters

Inputs B02B_HARDARM_L2_L_

EVAPORATION D3B02B_HARDARM_L2_L_

EVAPORATION D9 B02B_HARDARM_L2_L_

EVAPORATION E5B02B_HARDARM_L2_L_

EVAPORATION F2Chemical name (DIPPR)









Type of release



94 94 94 94


120 120 120 120


Height pool at t=0






19 19 19 19


1364 1364 1364 1364





19 19 19 19


500 500 500 500


3 9 5 2


19 19 19 19


75 75 75 75




100 100 100 100

Cloud cover (%)

Date: day number

Date: month number

Date: year number


Type of subsoil


Maximum evaluatio

1800 1800 1800 1800



n time for evaporation (s)

Results

B02B_HARDARM_L2_L_EVAPORATION D3

B02B_HARDARM_L2_L_EVAPORATION D9

B02B_HARDARM_L2_L_EVAPORATION E5

B02B_HARDARM_L2_L_EVAPORATION F2

Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1


35,5 35,5 35,5 35,5


65,5 65,5 65,5 65,5


276,1 276,1 276,1 276,1


41,024 41,024 41,024 41,024


-161,49 -161,49 -161,49 -161,49


30,215 30,215 30,215 30,215


1,7175 1,5907 1,6669 1,7473


11327 11327 11327 11327


65,5 65,5 65,5 65,5

Corresponding represen

717,01 717,01 717,01 717,01



tative pool surface area (m2) Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


ATMOSPHERIC DISPERSION Case description: B02B_HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/07/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B02B_HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION D9) compared to: B02B_HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION E5) compared to: B02B_HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION F2) Parameters

Inputs

B02B_HARDARM_L2_L_DISPERSION D3 (linked

to Pool evaporation -B02B_HARDARM_L2_L_

EVAPORATION D3)



EVAPORATION D9)

B02B_HARDARM_L2_L_DISPERSION E5 (linked


EVAPORATION E5)

B02B_HARDARM_L2_L_DISPERSION F2 (linked


EVAPORATION F2)Chemical name (DIPPR)


Type of release




276,1 276,1 276,1 276,1


41,024 41,024 41,024 41,024



717,01 717,01 717,01 717,01

Diamete



r of expanded jet (m) Temperature after release (°C)

-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75





Time t after start release (s)

120 120 120 120


20 20 20 20


Low Low Low Low

Results



EVAPORATION D3)



EVAPORATION D9)

B02B_HARDARM_L2_L_DISPERSION E5 (linked


EVAPORATION E5)

B02B_HARDARM_L2_L_DISPERSION F2 (linked


EVAPORATION F2)Explosive mass at time t (kg)

0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


9394,5 6486,1 8413,1 8961,6

...at time tmem (s)

45 45 40 60

Start time where 95% of maximum of explosiv

42,158 43,098 36,939 -1E100



e mass is reached (s) Time where explosive mass starts decreasing below 95% of max (s)

48,219 45,364 45,219 41,024


88,49 323,78 114,97 171,61


109,21 46,432 81,54 126,01


-10,125 -12,639 -18,568 -57,713


7485,8 12769 7738,4 18153

...at time tmac (s)

45 45 41,024 60


9394,5 6486,1 8413,1 8961,6


88,49 323,78 114,97 171,61


109,21 46,432 81,54 126,01

Offset between release

-10,125 -12,639 -18,568 -57,713



location and LEL at time tmac (m) Offset between release centre and cloud centre at time tmac (m)

34,12 149,25 38,915 28,09


0 0 0,011686 0,04733



EXPLOSION Case description: B02B_HARDARM_L2_L_UVCE D3 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02B_HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B02B_HARDARM_L2_L_UVCE D9 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02B_HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION D9)) compared to: B02B_HARDARM_L2_L_UVCE E5 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02B_HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION E5)) compared to: B02B_HARDARM_L2_L_UVCE F2 LC1 (linked to Dense Gas Dispersion: Explosive mass - B02B_HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - B02B_HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs

B02B_HARDARM_L2_L_UVCE D3 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02B_HARDARM_L2_L_DISPERSION D3 (linked


EVAPORATION D3))




EVAPORATION D9))

B02B_HARDARM_L2_L_UVCE E5 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02B_HARDARM_L2_L_DISPERSION E5 (linked


EVAPORATION E5))

B02B_HARDARM_L2_L_UVCE F2 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02B_HARDARM_L2_L_DISPERSION F2 (linked


EVAPORATION F2))Chemical name (DIPPR)


Ambient

1,0151 1,0151 1,0151 1,0151



pressure (bar) Total mass in explosive range (kg)

9394,5 6486,1 8413,1 8961,6


8 8 8 8

Curve number



100 100 100 100


34,12 149,25 38,915 28,09


100 100 100 100


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results





B02B_HARDARM_L2_L_UVCE E5 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02B_HARDARM_L2_L_DISPERSION E5 (linked

B02B_HARDARM_L2_L_UVCE F2 LC1 (linked to Dense Gas Dispersion:

Explosive mass -B02B_HARDARM_L2_L_DISPERSION F2 (linked




EVAPORATION D3))


EVAPORATION D9))


EVAPORATION E5))


EVAPORATION F2))Confined mass in explosive range (kg)

751,56 518,88 673,04 716,93


37601 25960 33673 35869


87,681 77,635 84,528 86,319


6,4508 4,9007 5,9427 6,2285


641,48 504,02 596,73 621,96


146,32 129,84 141,19 144,11


87,634 77,453 84,469 86,267









Habitable after relatively easy repairs. Minor

structural damage (3 kPa).







Damage to







typical American-style houses at Xd























POOL FIRE Case description: B02B_HARDARM_L2_L_PFIRE D3 Model: Pool fire version: 5.11 (27/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B02B_HARDARM_L2_L_PFIRE D9 compared to: B02B_HARDARM_L2_L_PFIRE E5 compared to: B02B_HARDARM_L2_L_PFIRE F2 Parameters

Inputs B02B_HARDARM_L2_L

_PFIRE D3B02B_HARDARM_L2_L

_PFIRE D9B02B_HARDARM_L2_L

_PFIRE E5B02B_HARDARM_L2_L

_PFIRE F2Chemical name (DIPPR)






94 94 94 94


120 120 120 120



0 0 0 0

Height of



the confined pool above ground level (m) Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35

Soot Fraction




9 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03

Distance from the

1000 1000 1000 1000



centre of the pool (m) Exposure duration to heat radiation (s)

75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4

Percentage of mortality for contour calculation



s (%)

Results

B02B_HARDARM_L2_L_PFIRE D3

B02B_HARDARM_L2_L_PFIRE D9

B02B_HARDARM_L2_L_PFIRE E5

B02B_HARDARM_L2_L_PFIRE F2

Max Diameter of the Pool Fire (m)

36,073 36,073 36,073 36,073


0,0075699 0,0075699 0,0093922 0,012103


70,774 70,774 73,027 71,004


64,958 64,958 65,985 62,112


58,268 58,268 57,668 51,717


79,715 79,715 79,715 79,715


141,5 141,5 141,5 141,5


72,354 72,354 67,033 62,271

Flame tilt (deg)

57,602 57,602 50,022 36,175

View factor (%)

0,022654 0,022654 0,030767 0,043259


46,183 46,183 45,54 44,931


791,19 791,19 771,17 752,23


34,696 34,696 39,254 44,222


1022 1022 1022 1022


0 0 0 0


0 0 0 0




0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69





B.03a– FSU UNLOADING ARM - LNG (RELEASE ON WATER) POOL EVAPORATION Case description: B03a EVAP D3 Model: Pool evaporation version: 5.16 (25/07/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B03a EVAP D9 compared to: B03a EVAP E5 compared to: B03a EVAP F2 Parameters Inputs B03a EVAP D3 B03a EVAP D9 B03a EVAP E5 B03a EVAP F2Chemical name (DIPPR) METHANE (DIPPR)METHANE (DIPPR)METHANE (DIPPR)METHANE (DIPPR)

Use which representative step First 20% average

(flammable)First 20% average



(flammable)Evaporation from land or water Water Water Water WaterType of release Continuous Continuous Continuous ContinuousMass flow rate of the source (kg/s)

353 353 353 353

Duration of the release (s) 120 120 120 120Total mass released (kg) Height pool at t=0 Value pool height at t=0 (m) Type of pool growth on Land

Type of pool growth on Water Confined water

surfaceConfined water



surfaceTemperature of the pool (°C) -161,15 -161,15 -161,15 -161,15Maximum pool surface area (m2)

10000 10000 10000 10000

Temperature of the subsoil (°C) Temperature of the water (°C) 14,4 14,4 14,4 14,4Max temperature difference between pool and water (K)

500 500 500 500

Wind speed at 10 m height (m/s) 3 9 5 2Ambient temperature (°C) 14,4 14,4 14,4 14,4Ambient relative humidity (%) 77 77 77 77Solar radiation flux User defined User defined User defined User definedSolar heat radiation flux (W/m2) 100 100 100 100Cloud cover (%) Date: day number Date: month number Date: year number Latitude of the location (deg) Type of subsoil Subsoil roughness description Maximum evaluation time for evaporation (s)

1800 1800 1800 1800

Results B03a EVAP D3 B03a EVAP D9 B03a EVAP E5 B03a EVAP F2Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1

Time pool spreading ends (s) 84 84 84 84Time until pool has totally evaporated (s)

84 84 84 84


774,5 774,5 774,5 774,5


54,938 54,938 54,938 54,938

Representative temperature (°C) -161,49 -161,49 -161,49 -161,49Representative pool diameter (m)

105,61 105,61 105,61 105,61


1,7001 1,5649 1,6444 1,734

Total evaporated mass (kg) 42550 42550 42550 42550



... duration evaporation time (s) 84 84 84 84Corresponding representative pool surface area (m2)

8759,1 8759,1 8759,1 8759,1



ATMOSPHERIC DISPERSION Case description: HARDARM_L1_L_DISPERSION D3 REV (linked to Pool evaporation - Case description: B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/07/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9) compared to: B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5) compared to: B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2) Parameters

Inputs B03a DISP D3 (linked to Pool evaporation -

B03a EVAP D3)

B03a DISP D9 (linked to Pool evaporation -

B03a EVAP D9)

B03a DISP E5 (linked to Pool evaporation -

B03a EVAP E5)

B03a DISP F2 (linked to Pool evaporation -

B03a EVAP F2)Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Type of release Evaporating pool

releaseEvaporating pool


release Evaporating pool

releaseTotal mass released (kg) Mass flow rate of the source (kg/s)

774,5 774,5 774,5 774,5


54,938 54,938 54,938 54,938


Fixed pool surface (m2) 8759,1 8759,1 8759,1 8759,1Diameter of expanded jet (m)


-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data Pasquill Pasquill Pasquill PasquillPasquill stability class D (Neutral) D (Neutral) E (Stable) F (Very Stable)Wind speed at 10 m height (m/s)

3 9 5 2


Predefined wind direction User defined User defined User defined User definedWind comes from (North = 0 degrees) (deg)

270 270 270 270


75 75 75 75


Regular large obstacle coverage






(suburb or forest). (suburb or forest). (suburb or forest). (suburb or forest).Time t after start release (s)

120 120 120 120


20 20 20 20


Low Low Low Low

Results B03a DISP D3 (linked to Pool evaporation -

B03a EVAP D3)

B03a DISP D9 (linked to Pool evaporation -

B03a EVAP D9)

B03a DISP E5 (linked to Pool evaporation -

B03a EVAP E5)

B03a DISP F2 (linked to Pool evaporation -

B03a EVAP F2)Explosive mass at time t (kg)

7228,8 0 0 28734


21,7 0 0 27


208,55 0 0 302,55


85,284 0 0 91,93


234,22 0 0 13,807


24411 8987,6 29489 32372

...at time tmem (s) 50 30 60 75Start time where 95% of maximum of explosive mass is reached (s)

-1E100 24,509 50,255 -1E100


54,938 54,938 61,44 54,938


235,09 293,33 183,64 242,62


150,49 121,52 162,02 108,9


-17,351 -55,127 -11,818 -40,724


29801 28143 31642 52817

...at time tmac (s) 50 54,938 54,938 300Explosive mass at time tmac (kg)

24411 8985,2 27975 8896,7


235,09 296,96 218,62 392,69


150,49 121,03 160,9 169,42


-17,351 -55,127 -61,747 318,66


100,19 93,352 47,564 515,01


0 0 0,0081 0,0385





EXPLOSION Case description: B03a UVCE D3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03a UVCE D9 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9)) compared to: B03a UVCE E5 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE F2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) Parameters

Inputs

B03a UVCE D3 (linked to Dense Gas Dispersion: Explosive mass - B03a

DISP D3 (linked to Pool evaporation - B03a EVAP

D3))

B03a UVCE D9 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9

(linked to Pool evaporation - B03a

EVAP D9))

B03a UVCE E5 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool

evaporation - B03a EVAP E5))

B03a UVCE F2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2


EVAP F2))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


24411 8985,2 27975 8896,7


8 8 8 8

Curve number 5 (Medium deflagration)5 (Medium

deflagration)5 (Medium deflagration)

5 (Medium deflagration)


50 50 50 50


100,19 93,352 47,564 515,01


100 100 100 100


0 0 0 0


0 0 0 0




270 270 270 270

Results

B03a UVCE D3 (linked to Dense Gas Dispersion: Explosive mass - B03a

DISP D3 (linked to Pool evaporation - B03a EVAP

D3))

B03a UVCE D9 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9


EVAP D9))

B03a UVCE E5 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool


B03a UVCE F2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2


EVAP F2))




1952,9 718,82 2238 711,74


97704 35963 1,1197E05 35609


206,07 172,41 206,07 171,84


66,176 31,564 72,107 31,353


2138,5 1210,6 2277,9 1202,7


207,55 140,44 221,08 139,98


120,48 86,342 126,08 86,058





Moderate damage (Zone C: 17 - 35

kPa).



kPa).


Not habitable without major repair works. Partial roof failures, 25% of all brick

walls have failed, serious damage to the remaining

carrying elements. Damage to windowframes

and doors (7-15 kPa).

Not habitable without major repair works. Partial roof failures,

25% of all brick walls have failed, serious

damage to the remaining carrying

elements. Damage to windowframes and

doors (7-15 kPa).



carrying elements. Damage to windowframes






doors (7-15 kPa).



and doors; failure of joints. Doors and window frames have failed. Wall covering has fallen down (15 kPa).


walls and doors; failure of joints. Doors

and window frames have failed. Wall



and doors; failure of joints. Doors and window frames have failed. Wall covering has fallen down (15 kPa).






Collapse of steel frames and displacement of foundation (20 kPa).

Industrial steel self-framing structure collapsed (20-30

kPa). Cracking in empty oil-storage tanks (20-30

kPa). Slight deformation of a pipe-bridge (20-30 kPa).

Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel

Walls made of concrete blocks

have collapsed (15-20). Minor damage


between steel or aluminium

ondulated plates have failed 7-14

kPa). The roof of a storage tank has

collapsed (7 kPa).



kPa). Cracking in empty oil-storage tanks (20-30

kPa). Slight deformation of a pipe-bridge (20-30 kPa).








collapsed (7 kPa).



frames (8-10 kPa). Connections between steel

or aluminium ondulated plates have failed 7-14

kPa). The roof of a storage tank has collapsed (7 kPa).






POOL FIRE Case description: B03a PFIRE D3 Model: Pool fire version: 5.11 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B03a PFIRE D9 compared to: B03a PFIRE E5 compared to: B03a PFIRE F2 Parameters Inputs B03a PFIRE D3 B03a PFIRE D9 B03a PFIRE E5 B03a PFIRE F2

Chemical name (DIPPR) METHANE

(DIPPR)METHANE

(DIPPR)METHANE

(DIPPR)METHANE

(DIPPR)Pool size determination Confined Confined Confined ConfinedTotal mass released (kg) 42630 42630 42630 42630Mass flow rate of the source (kg/s) Duration of the release (s) Pool surface poolfire (m2) 10000 10000 10000 10000Height of the observer position above ground level (m)

0 0 0 0


0 0 0 0

Hole diameter (mm) Discharge coefficient (-) Initial height of the liquid above release point (m)

Cross-sectional area of the tank (m2) Pool thickness (mm) Temperature of the pool (°C) -161,15 -161,15 -161,15 -161,15Pool burning rate Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of pool burning rate (kg/m2*s) Fraction combustion heat radiated (%) 35 35 35 35Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of soot fraction (-) Wind speed at 10 m height (m/s) 3 9 5 2Ambient temperature (°C) 19 19 19 19Ambient relative humidity (%) 75 75 75 75Amount of CO2 in atmosphere (%) 0,03 0,03 0,03 0,03Distance from the centre of the pool (m)

1000 1000 1000 1000

Exposure duration to heat radiation (s) 20 20 20 20Take protective effects of clothing into account

No No No No

X-coordinate of release (m) 0 0 0 0Y-coordinate of release (m) 0 0 0 0Predefined wind direction User defined User defined User defined User definedWind comes from (North = 0 degrees) 270 270 270 270



(deg) Calculate all contours for Physical effects Physical effects Physical effects Physical effectsHeat radiation level (lowest) for first contour plot (kW/m2)

6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4


Results B03a PFIRE D3 B03a PFIRE D9 B03a PFIRE E5 B03a PFIRE F2Max Diameter of the Pool Fire (m) 112,84 112,84 112,84 112,84Heat radiation at X (kW/m2) 0,11465 0,083056 0,10169 0,12194Heat radiation first contour at (m) 198,96 193,87 200,39 195,03Heat radiation second contour at (m) 177,63 177,35 181,02 172,64Heat radiation third contour at (m) 153,44 159,19 159,19 147,33Combustion rate (kg/s) 780 780 780 780Duration of the pool fire (s) 54,654 54,654 54,654 54,654Heat emission from fire surface (kW/m2)

78,846 87,066 80,77 78,846

Flame tilt (deg) 37,614 53,697 45,489 31,201View factor (%) 0,30773 0,19824 0,26527 0,32729Atmospheric transmissivity (%) 47,253 48,121 47,462 47,253Flame temperature (°C) 814,17 841,32 820,71 814,17Height of the Flame (m) 94,407 80,225 90,764 94,407Calculated pool surface area (m2) 10000 10000 10000 10000Weight ratio of HCL/chemical (%) 0 0 0 0Weight ratio of NO2/chemical (%) 0 0 0 0Weight ratio of SO2/chemical (%) 0 0 0 0Weight ratio of CO2/chemical (%) 274,4 274,4 274,4 274,4Weight ratio of H2O/chemical (%) 224,69 224,69 224,69 224,69 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.03b– FSU UNLOADING AR, - LNG (RELEASE ON WATER) POOL EVAPORATION Case description: B03b EVAP D3 Model: Pool evaporation version: 5.16 (25/07/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B03b EVAP D9 compared to: B03b EVAP E5 compared to: B03b EVAP F2 Parameters Inputs B03b EVAP D3 B03b EVAP D9 B03b EVAP E5 B03b EVAP F2Chemical name (DIPPR) METHANE (DIPPR)METHANE (DIPPR)METHANE (DIPPR)METHANE (DIPPR)

Use which representative step First 20% average




(flammable)Evaporation from land or water Water Water Water WaterType of release Continuous Continuous Continuous ContinuousMass flow rate of the source (kg/s)

2,18 2,18 2,18 2,18

Duration of the release (s) 120 120 120 120Total mass released (kg) Height pool at t=0 Value pool height at t=0 (m) Type of pool growth on Land

Type of pool growth on Water Confined water




surfaceTemperature of the pool (°C) -161,15 -161,15 -161,15 -161,15Maximum pool surface area (m2)

62 62 62 62

Temperature of the subsoil (°C) Temperature of the water (°C) 14,4 14,4 14,4 14,4Max temperature difference between pool and water (K)

500 500 500 500

Wind speed at 10 m height (m/s) 3 9 5 2Ambient temperature (°C) 14,4 14,4 14,4 14,4Ambient relative humidity (%) 77 77 77 77Solar radiation flux User defined User defined User defined User definedSolar heat radiation flux (W/m2) 100 100 100 100Cloud cover (%) Date: day number Date: month number Date: year number Latitude of the location (deg) Type of subsoil Subsoil roughness description Maximum evaluation time for evaporation (s)

1800 1800 1800 1800

Results B03b EVAP D3 B03b EVAP D9 B03b EVAP E5 B03b EVAP F2Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1

Time pool spreading ends (s) 16 16 16 16Time until pool has totally evaporated (s)

19 19 19 19


36,671 36,671 36,671 36,671


7,2048 7,2048 7,2048 7,2048

Representative temperature (°C) -161,49 -161,49 -161,49 -161,49Representative pool diameter (m)

8,8849 8,8849 8,8849 8,8849


1,6365 1,4807 1,5668 1,6833

Total evaporated mass (kg) 264,2 264,2 264,2 264,2



... duration evaporation time (s) 19 19 19 19Corresponding representative pool surface area (m2)

62 62 62 62


DISPERSION Case description: B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/07/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9) compared to: B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5) compared to: B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2) Parameters

Inputs B03b DISP D3 (linked to Pool evaporation -

B03b EVAP D3)

B03b DISP D9 (linked to Pool evaporation -

B03b EVAP D9)

B03b DISP E5 (linked to Pool evaporation -

B03b EVAP E5)

B03b DISP F2 (linked to Pool evaporation -

B03b EVAP F2)Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)





releaseTotal mass released (kg) Mass flow rate of the source (kg/s)

36,671 36,671 36,671 36,671


7,2048 7,2048 7,2048 7,2048


Fixed pool surface (m2) 62 62 62 62Diameter of expanded jet (m)


-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



14,4 14,4 14,4 14,4


3 9 5 2


Predefined wind direction User defined User defined User defined User definedWind comes from (North = 0 degrees) (deg)

270 270 270 270


77 77 77 77


Regular large obstacle coverage (suburb or forest).





120 120 120 120


20 20 20 20




Low Low Low Low

Results B03b DISP D3 (linked to Pool evaporation -

B03b EVAP D3)

B03b DISP D9 (linked to Pool evaporation -

B03b EVAP D9)

B03b DISP E5 (linked to Pool evaporation -

B03b EVAP E5)

B03b DISP F2 (linked to Pool evaporation -

B03b EVAP F2)Explosive mass at time t (kg)

0 0 0 -1E100


0 0 0 -1E100


0 0 0 -1E100


0 0 0 -1E100


0 0 0 -1E100


196,31 180,62 194,24 -1E100

...at time tmem (s) 7,5 7 7,5 -1E100Start time where 95% of maximum of explosive mass is reached (s)

-1E100 6,4346 -1E100 -1E100


7,2048 8,2784 7,2048 -1E100


27,474 34,656 33,691 -1E100


14,767 14,82 14,773 -1E100


-6,6877 -5,2709 -5,6714 -1E100


401,46 495,91 478,28 -1E100

...at time tmac (s) 15 8 12,5 -1E100Explosive mass at time tmac (kg)

152,77 179,75 151,83 0


36,114 38,845 43,125 -1E100


13,786 15,198 13,769 -1E100


1,9316 -1,695 2,7495 -1E100


19,989 17,728 24,312 -1,5E100


0 0 0,0081 0



EXPLOSION Case description: B03b UVCE D3 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3))



Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03b UVCE D9 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE E5 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5)) compared to: B03b UVCE F2 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) Parameters

Inputs

B03b UVCE D3 (linked to Dense Gas

Dispersion: Explosive mass - B03b DISP D3

(linked to Pool evaporation - B03b

EVAP D3))




EVAP D9))

B03b UVCE E5 (linked to Dense Gas

Dispersion: Explosive mass - B03b DISP E5


EVAP E5))

B03b UVCE F2 (linked to Dense Gas

Dispersion: Explosive mass - B03b DISP F2





1,0151 1,0151 1,0151 1,0151


152,77 179,75 151,83 0


8 8 8 8

Curve number 5 (Medium deflagration)5 (Medium deflagration)5 (Medium deflagration) 5 (Medium deflagration)Distance from release (Xd) (m)

50 50 50 50


19,989 17,728 24,312 -1,5E100


100 100 100 100


0 0 0 0


0 0 0 0




270 270 270 270

Results




EVAP D3))




EVAP D9))

B03b UVCE E5 (linked to Dense Gas

Dispersion: Explosive mass - B03b DISP E5


EVAP E5))

B03b UVCE F2 (linked to Dense Gas

Dispersion: Explosive mass - B03b DISP F2


EVAP F2))Confined mass in explosive range (kg)

12,222 14,38 12,147 0


611,48 719,46 607,7 -1E94


44,536 47,613 44,432 -1E98

Peak dynamic pressure at Xd

1,2367 1,4296 1,2296 -1E98



(mbar) Pressure impulse at Xd (Pa*s)

85,25 96,169 84,877 -1E100


38,284 40,396 38,206 -1E103


22,202 23,439 22,156 -1E100


Pressure wave Pressure wave Pressure wave *** NOT INITIALIZED











Habitable afterrelatively easy repairs.















POOL FIRE Case description: B03b PFIRE D3 Model: Pool fire version: 5.11 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B03b PFIRE D9 compared to: B03b PFIRE E5 compared to: B03b PFIRE F2 Parameters Inputs B03b PFIRE D3 B03b PFIRE D9 B03b PFIRE E5 B03b PFIRE F2

Chemical name (DIPPR) METHANE

(DIPPR)METHANE

(DIPPR)METHANE

(DIPPR)METHANE

(DIPPR)Pool size determination Confined Confined Confined ConfinedTotal mass released (kg) 261,6 261,6 261,6 261,6Mass flow rate of the source (kg/s) Duration of the release (s) Pool surface poolfire (m2) 62 62 62 62Height of the observer position above ground level (m)

0 0 0 0


0 0 0 0


Cross-sectional area of the tank (m2) Pool thickness (mm)



Temperature of the pool (°C) -161,15 -161,15 -161,15 -161,15Pool burning rate Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of pool burning rate (kg/m2*s) Fraction combustion heat radiated (%) 35 35 35 35Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of soot fraction (-) Wind speed at 10 m height (m/s) 3 9 5 2Ambient temperature (°C) 19 19 19 19Ambient relative humidity (%) 75 75 75 75Amount of CO2 in atmosphere (%) 0,03 0,03 0,03 0,03Distance from the centre of the pool (m)

1000 1000 1000 1000

Exposure duration to heat radiation (s) 20 20 20 20Take protective effects of clothing into account

No No No No

X-coordinate of release (m) 0 0 0 0Y-coordinate of release (m) 0 0 0 0Predefined wind direction User defined User defined User defined User definedWind comes from (North = 0 degrees) (deg)

270 270 270 270

Calculate all contours for Physical effects Physical effects Physical effects Physical effectsHeat radiation level (lowest) for first contour plot (kW/m2)

6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4


Results B03b PFIRE D3 B03b PFIRE D9 B03b PFIRE E5 B03b PFIRE F2Max Diameter of the Pool Fire (m) 8,8849 8,8849 8,8849 8,8849Heat radiation at X (kW/m2) 0,0006517 0,00042763 0,00053985 0,00074604Heat radiation first contour at (m) 21,649 21,422 21,932 20,839Heat radiation second contour at (m) 18,814 19,233 19,345 17,859Heat radiation third contour at (m) 15,53 17,552 16,941 13,998Combustion rate (kg/s) 4,836 4,836 4,836 4,836Duration of the pool fire (s) 54,094 54,094 54,094 54,094Heat emission from fire surface (kW/m2)

50,042 57,532 53,369 47,584

Flame tilt (deg) 48,267 61,915 55,145 42,233View factor (%) 0,003 0,0016828 0,0023132 0,0036322Atmospheric transmissivity (%) 43,41 44,17 43,728 43,165Flame temperature (°C) 698,08 732,27 713,71 686,03Height of the Flame (m) 15,603 12,388 14,016 16,99Calculated pool surface area (m2) 62 62 62 62Weight ratio of HCL/chemical (%) 0 0 0 0Weight ratio of NO2/chemical (%) 0 0 0 0Weight ratio of SO2/chemical (%) 0 0 0 0Weight ratio of CO2/chemical (%) 274,4 274,4 274,4 274,4Weight ratio of H2O/chemical (%) 224,69 224,69 224,69 224,69 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.04a GAS TANKER UNLOADING ARM - GAS RETURN TO GAS TANKER JET FIRE Case description: B04a_D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/07/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B04a_D9 compared to: B04a_E5 compared to: B04a_F2 Parameters Inputs B04a_D3 B04a_D9 B04a_E5 B04a_F2Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Type of release Release from vessel

through (a hole in) pipe

Release from vessel through (a hole in)

pipe


pipe


pipePipeline length (m) 30 30 30 30Pipeline diameter (inch) 12 12 12 12Pipeline roughness (mm) 0,045 0,045 0,045 0,045Hole diameter (inch) 12 12 12 12Hole rounding Rounded edges Rounded edges Rounded edges Rounded edgesDischarge coefficient (-) 1 1 1 1Initial temperature in vessel (°C)

-151 -151 -151 -151

Initial (absolute) pressure in vessel (bar)

1,03 1,03 1,03 1,03

Outflow angle in XZ plane (0°=horizontal; 90°=vertical) (deg)

45 45 45 45

Release height (Stack height) (m)

1 1 1 1


3 9 5 2

Ambient temperature (°C) 19 19 19 19Ambient relative humidity (%)

75 75 75 75

Flame temperature (°C) 926,85 926,85 926,85 926,85Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03

Percentage of the flame covered by soot (%)

0 0 0 0


100 100 100 100


270 270 270 270

Results B04a_D3 B04a_D9 B04a_E5 B04a_F2Initial source strength (kg/s) 3,3751 3,3751 3,3751 3,3751Type of flow of the jet Unchoked flow Unchoked flow Unchoked flow Unchoked flowExit velocity of expanding jet (m/s)

28,824 28,824 28,824 28,824

Angle between hole and flame axis (alpha) (deg)

0 16,056 1,5266 0

Frustum lift off height (b) (m) 6,21 0,37833 0,55996 6,939Width of frustum base (W1) (m)

3,0683 1,256 2,203 3,6564

Width of frustum tip (W2) (m)

13,905 10,274 12,028 15,024

Length of frustum (flame) (Rl) (m)

24,84 23,948 26,409 27,756



Tilt angle central axis flare (alpha_b) (deg)

0 15,81 1,4949 0

Surface area of frustum (m2)

837,08 525,5 717,94 1019,1

Surface area of a cylinder (m2)

775,4 485,94 669,9 951,5

Surface emissive power (max) (kW/m2)

65,622 104,71 75,956 53,477

Surface emissive power (actual) (kW/m2)

65,622 104,71 75,956 53,477


68,48 68,1 68,157 68,545

View factor (%) 0,86995 0,42126 0,68539 1,1076Heat radiation at Xd (kW/m2)

0,39164 0,30183 0,3556 0,40675



DISPERSION Case description: B04a_DISP D3 (linked to Gas Jet Fire (Chamberlain model) - B04a_D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B04a_DISP D9 (linked to Gas Jet Fire (Chamberlain model) - B04a_D9) compared to: B04a_DISP E5 (linked to Gas Jet Fire (Chamberlain model) - B04a_E5) compared to: B04a_DISP F2 (linked to Gas Jet Fire (Chamberlain model) - B04a_F2) Parameters

Inputs

B04a_DISP D3 (linked to Gas Jet Fire

(Chamberlain model) -B04a_D3)


(Chamberlain model) - B04a_D9)

B04a_DISP E5 (linked to Gas Jet Fire

(Chamberlain model) -B04a_E5)

B04a_DISP F2 (linked to Gas Jet Fire

(Chamberlain model) -B04a_F2)



Type of release Continuous Continuous Continuous ContinuousTotal mass released (kg)


3,3751 3,3751 3,3751 3,3751



0 0 0 0


0 0 0 0


0 0 0 0

Length source in wind (x) direction (m)

0 0 0 0

Length source in crosswind (y) direction (m)

0 0 0 0

Length source in vertical (z) direction (m)

0 0 0 0

Ambient temperature 19 19 19 19



(°C) Meteorological data Pasquill Pasquill Pasquill PasquillPasquill stability class D (Neutral) D (Neutral) E (Stable) F (Very Stable)Wind speed at 10 m height (m/s)

3 9 5 2


51 51 51 51


Mixing height (m) Stand. dev. of turbulent velocity in vertical direction (m/s)

Stand. dev. of turbulent velocity in horizontal direction (m/s)


Regular large obstacle coverage (suburb or

forest).


forest).


forest).


forest).Predefined wind direction



270 270 270 270



20 20 20 20

Integration tolerance (%)

0,1 0,1 0,1 0,1


Results


(Chamberlain model) -B04a_D3)


(Chamberlain model) - B04a_D9)

B04a_DISP E5 (linked to Gas Jet Fire

(Chamberlain model) -B04a_E5)

B04a_DISP F2 (linked to Gas Jet Fire

(Chamberlain model) -B04a_F2)

Total explosive mass (kg)

28,278 4,6123 18,915 156,73

Height to LEL (m) 5,6 3,6 4,1 5,3Length of cloud (between LEL) (m)

43,9 21,44 49,14 165,58

Width of cloud (between LEL) (m)

3,2411 1,6943 2,6787 5,202

Offset between release location and LEL (m)

0,01 0,01 0,01 0,01


114,16 29,442 105,01 675,41


28,278 4,6123 18,915 156,73


0 0 0,0083197 0,050692

Mixing height used (m)

500 500 361,02 70,689

Stand. dev. of turbulent velocity in vert. direction used (m/s)

1,0135 3,0406 1,455 0,3399



Stand. dev. of turbulent velocity in horiz. direction used (m/s)

0,69649 2,0895 0,99553 0,23256





B.04b– GAS TANKER UNLOADING ARM - GAS RETURN TO GAS TANKER JET FIRE Case description: B04b_D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/07/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B04b_D9 compared to: B04b_E5 compared to: B04b_F2 Parameters Inputs B04b_D3 B04b_D9 B04b_E5 B04b_F2Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)




pipe


pipe


pipePipeline length (m) 30 30 30 30Pipeline diameter (inch) 12 12 12 12Pipeline roughness (mm) 0,045 0,045 0,045 0,045Hole diameter (inch) 1,2 1,2 1,2 1,2Hole rounding Sharp edges Sharp edges Sharp edges Sharp edgesDischarge coefficient (-) 0,62 0,62 0,62 0,62Initial temperature in vessel (°C)

-151 -151 -151 -151


1,03 1,03 1,03 1,03


45 45 45 45


1 1 1 1


3 9 5 2


75 75 75 75

Flame temperature (°C) 926,85 926,85 926,85 926,85Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


270 270 270 270

Results B04b_D3 B04b_D9 B04b_E5 B04b_F2Initial source strength (kg/s) 0,031678 0,031678 0,031678 0,031678Type of flow of the jet Unchoked flow Unchoked flow Unchoked flow Unchoked flowExit velocity of expanding jet (m/s)

43,589 43,589 43,589 43,589


13,762 45,337 24,724 7,0413


0,28874 0,14976 0,22924 0,32522


1,8063 1,4413 1,6291 1,8973


3,9221 3,2229 3,5117 4,2524




12,913 44,522 23,891 6,4154


15,774 9,8636 12,578 18,008


14,631 9,0485 11,607 16,786


31,677 51,219 39,929 27,611


31,677 51,219 39,929 27,611


67,926 67,907 67,915 67,936


0,0021096 0,00060349 0,0016465 0,0023513



DISPERSION Case description: B04b_DISP D3 (linked to Gas Jet Fire (Chamberlain model) - B04b_D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B04b_DISP D9 (linked to Gas Jet Fire (Chamberlain model) - B04b_D9) compared to: B04b_DISP E5 (linked to Gas Jet Fire (Chamberlain model) - B04b_E5) compared to: B04b_DISP F2 (linked to Gas Jet Fire (Chamberlain model) - B04b_F2) Parameters

Inputs

B04b_DISP D3 (linked to Gas Jet Fire

(Chamberlain model) -B04b_D3)


(Chamberlain model) - B04b_D9)

B04b_DISP E5 (linked to Gas Jet Fire

(Chamberlain model) -B04b_E5)

B04b_DISP F2 (linked to Gas Jet Fire

(Chamberlain model) -B04b_F2)





0,031678 0,031678 0,031678 0,031678



0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


19 19 19 19




3 9 5 2


51 51 51 51






forest).


forest).


forest).


forest).Predefined wind direction



270 270 270 270



20 20 20 20


0,1 0,1 0,1 0,1


Results


(Chamberlain model) -B04b_D3)


(Chamberlain model) - B04b_D9)

B04b_DISP E5 (linked to Gas Jet Fire

(Chamberlain model) -B04b_E5)

B04b_DISP F2 (linked to Gas Jet Fire

(Chamberlain model) -B04b_F2)

Total explosive mass (kg)

0,010994 0,0015793 0,0068689 0,056588

Height to LEL (m) 0,9 0,6 0,7 1Length of cloud (between LEL) (m)

1,8925 0,85125 1,9875 6,44

Width of cloud (between LEL) (m)

0,1924 0,09623 0,15108 0,28035

Offset between release location and LEL (m)

0,01 0,01 0,01 0,01


0,30859 0,070441 0,254 1,4962


0,010994 0,0015793 0,0068689 0,056588


0 0 0,0083197 0,050692


500 500 361,02 70,689


1,0135 3,0406 1,455 0,3399

Stand. dev. of 0,69649 2,0895 0,99553 0,23256



turbulent velocity in horiz. direction used (m/s) Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.05 PIPELINE FROM FSU TANK TO SECONDARY PUMP - SUCTION (RELEASE ON WATER) RELEASE Case description: A07_B05_C04_tank to compressor DISCHARGE - release Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (27/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Type of release Release from vessel through (a hole in) pipePipeline length (m) 26,5Pipeline diameter (m) 0,1016Hole diameter (inch) 4Height difference between pipe entrance and exit (m) 0Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 90000Vessel type Horizontal cylinderLength cylinder (m) 26,5Filling degree (%) 99Pressure inside vessel determination Use actual pressureInitial (absolute) pressure in vessel (bar) 28Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 3,8014E07Initial (vapour) pressure in vessel (bar) 28Time needed to empty vessel (s) 1,2263E06Massflowrate at end outflow (kg/s) 0Total mass released (kg) 3,6365E07Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -164,44VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 1,5248E06Vapour mass in vessel at end outflow (kg) 1,2446E05Height of liquid at end outflow (m) 5,4694Fillingdegree at end outflow (%) 3,969Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -164,44Maximum mass flow rate (kg/s) 228,97Representative release rate (kg/s) 217,35Representative outflow duration (s) 1800Representative temperature (°C) -161Representative pressure at exit (bar) 1,0565Representative vapour mass fraction (%) 0 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


POOL EVAPORATION Case description: tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release)



Model: Pool evaporation version: 5.16 (27/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) compared to: tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) compared to: tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) Parameters

Inputs

tank (secondary pump) to compressor -

evaporation D3 (linked to Liquefied Gas Bottom

Discharge (TPDIS model) -

A07_B05_C04_tank to compressor

DISCHARGE - release)







evaporation E5 (linked to Liquefied Gas Bottom





evaporation F2 (linked to Liquefied Gas Bottom



DISCHARGE - release)Chemical name (DIPPR)



Land Land Land Land

Type of release Continuous Continuous Continuous ContinuousMass flow rate of the source (kg/s)

217,35 217,35 217,35 217,35


1800 1800 1800 1800


3,6365E07 3,6365E07 3,6365E07 3,6365E07





19 19 19 19


1500 1500 1500 1500


3 9 5 2


100 100 100 100

Results




















DISCHARGE - release)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1

Time pool spreading ends

46,5 46,5 46,5 46,5



(s) Time until pool has totally evaporated (s)


48,642 56,312 49,419 49,044


1079,8 1325,6 1252,7 943,29


-161,49 -161,49 -161,49 -161,49


30,649 32,739 30,55 31,095


1,4928 1,3542 1,4206 1,5536


52524 74650 61910 46263


1799,5 1799,5 1799,5 1799,5


737,76 841,82 733,02 759,4



ATMOSPHERIC DISPERSION Case description: tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (27/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release)) compared to: tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release)) compared to: tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release)) Parameters

Inputs


dispersion D3 (linked to Pool evaporation - tank




dispersion E5 (linked to Pool evaporation - tank


dispersion F2 (linked to Pool evaporation - tank



(secondary pump) to compressor -




DISCHARGE - release))















DISCHARGE - release))Chemical name (DIPPR)


Type of release

Evaporating pool release





3,6365E07 3,6365E07 3,6365E07 3,6365E07


48,642 56,312 49,419 49,044


1079,8 1325,6 1252,7 943,29



737,76 841,82 733,02 759,4



-161,49 -161,49 -161,49 -161,49





3 9 5 2




1800 1800 1800 1800

Results
















dispersion E5 (linked to Pool evaporation - tank







dispersion F2 (linked to Pool evaporation - tank





DISCHARGE - release))Explosive mass at time

0 0 0 0



t (kg) Height to LEL at time t (m)

0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


1469,2 117,21 1312,5 3293,4

...at time tmem (s)

1000 500 400 400


95 95 95 97,293


1079,8 1325,6 1252,7 943,29


169,19 59,746 209,2 79,629


43,221 30,528 43,519 81,06


-17,651 -14,292 -17,462 -18,722


5508,9 1456,5 6168,3 5171,1

...at time tmac (s)

1079,8 1325,6 1252,7 943,29


1469,2 117,21 1312,5 3215,8

Length of cloud

169,19 14,284 209,2 79,629



(between LEL) at time tmac (m) Width of cloud (between LEL) at time tmac (m)

43,221 27,344 43,519 81,06


-17,651 -14,292 -17,462 -18,722


66,941 -7,1494 87,137 21,092


0 0 0,011686 0,04733



EXPLOSION Case description: tank (secondary pump) to compressor - uvce D3 LC1 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) Model: Explosion (Multi Energy model) version: 5.03 (27/06/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: tank (secondary pump) to compressor - uvce D9 LC1 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce D3 LC10 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce D3 LC50 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank



to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce D9 LC10 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce D9 LC50 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce E5 LC10 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce E5 LC50 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce F2 LC10 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) compared to: tank (secondary pump) to compressor - uvce F2 LC50 (linked to Dense Gas Dispersion: Explosive mass - tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release))) Parameters

Inputs

tank (second

ary pump) to compres

sor -uvce D3

LC1 (linked

to Dense

Gas Dispersi

on: Explosive mass -

tank (second


sor -dispersi

on D3 (linked to Pool

evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D3 (linked

tank (second


sor -uvce D9

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D9 (linked

tank (second


sor - uvce E5

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi

on E5 (linked to Pool

evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion E5 (linked

tank (second


sor -uvce F2

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi

on F2 (linked to Pool

evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion F2 (linked

tank (second


sor - uvce D3

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion D3 (linked

tank (second


sor -uvce D3

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D3 (linked

tank (second


sor -uvce D9

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D9 (linked

tank (second


sor - uvce D9

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion D9 (linked

tank (second


sor -uvce E5

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion E5 (linked

tank (second


sor -uvce E5

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion E5 (linked

tank (second


sor - uvce F2

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion F2 (linked

tank (second


sor -uvce F2

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion F2 (linked



to Liquefie

d Gas Bottom

Discharge

(TPDIS model) -A07_B05_C04_t

ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge

(TPDIS model) - A07_B05_C04_t

ank to compres

sor DISCHA

RGE - release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

)

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

)Chemical name (DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


1469,2 117,21 1312,5 3215,8 1469,2 1469,2 117,21 117,21 1312,5 1312,5 3215,8 3215,8


8 8 8 8 8 8 8 8 8 8 8 8

Curve number

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)

5 (Medium deflagrat

ion)Distance from release (Xd) (m)

50 50 50 50 50 50 50 50 50 50 50 50

Offset between release point and cloud

66,941 -7,1494 87,137 21,092 66,941 66,941 -7,1494 -7,1494 87,137 87,137 21,092 21,092



centre (m) Threshold overpressure (mbar)

100 100 100 100 300 942 300 942 300 942 300 942

Results

tank (second


sor -uvce D3

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D3 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor -uvce D9

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D9 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor - uvce E5

LC1 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion E5 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

tank (second


sor -uvce F2

LC1(linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion F2 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor - uvce D3

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion D3 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

tank (second


sor -uvce D3

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D3 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor -uvce D9

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion D9 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor - uvce D9

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion D9 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

tank (second


sor -uvce E5

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion E5 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor -uvce E5

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion E5 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))

tank (second


sor - uvce F2

LC10 (linked

to Dense

Gas Dispersi


tank (second


sor - dispersi


evaporation - tank

(secondary

pump) to compres

sor - evaporat

ion F2 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE - release))

tank (second


sor -uvce F2

LC50 (linked

to Dense

Gas Dispersi


tank (second


sor -dispersi


evaporation -tank

(secondary

pump) to compres

sor -evaporat

ion F2 (linked

to Liquefie

d Gas Bottom

Discharge


ank to compres

sor DISCHA

RGE -release))



) ) ) ) ) ) ) ) ) ) ) )Confined mass in explosive range (kg)

117,53 9,3765 105 257,26 117,53 117,53 9,3765 9,3765 105 105 257,26 257,26


5880,3 469,11 5253,2 12871 5880,3 5880,3 469,11 469,11 5253,2 5253,2 12871 12871


94,45 40,287 90,979 122,17 94,45 94,45 40,287 40,287 90,979 90,979 122,17 122,17


7,7911 1,0172 7,0921 14,36 7,7911 7,7911 1,0172 1,0172 7,0921 7,0921 14,36 14,36


371,46 70,656 345 617,09 371,46 371,46 70,656 70,656 345 345 617,09 617,09


78,658 35,076 75,841 101,02 78,658 78,658 35,076 35,076 75,841 75,841 101,02 101,02


47,214 20,325 45,472 61,302 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100

Blast-wave shap

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave



e at Xd Damage (general description) at Xd

Minor damage (Zone D: 3.5 - 17

kPa).


kPa).


kPa).


kPa).


kPa).

Minor damage (Zone D:3.5 - 17

kPa).


kPa).


kPa).


kPa).


kPa).


kPa).


kPa).


Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Not habitabl

e without

major repair

works. Partial

roof failures,

25% of all brick

walls have

failed, serious damage

to the remaini

ng carrying element

s. Damage

to windowframes


Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs.Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Not habitabl

e without

major repair

works. Partial

roof failures,

25% of all brick

walls have


to the remaini

ng carrying element

s. Damage

to windowframes


Not habitabl

e without

major repair

works. Partial

roof failures,

25% of all brick

walls have


to the remaini

ng carrying element

s. Damage

to windowframes



Minor damage. Compar

able to a damage due to a

storm; wooden

walls fail,

breakage of

windows (7-10 kPa).

No damage or very minor

damage



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).


damage


damage



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).



storm; wooden

walls fail,

breakage of

windows (7-10 kPa).

Damage to structures (empirical)

Minor damage to steel frames

(8-10 kPa).

Connecti


damage


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti


damage


damage


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti


(8-10 kPa).

Connecti



at Xd ons between steel or

aluminium

ondulated plates

have failed 7-14 kPa). The roof

of a storage

tank has collapse

d (7 kPa).

ons between steel or

aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).


aluminium

ondulated plates


of a storage

tank has collapse

d (7 kPa).



POOL FIRE Case description: tank (secondary pump) to compressor - PFIRE D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) Model: Pool fire version: 5.11 (27/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: tank (secondary pump) to compressor - PFIRE D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) compared to: tank (secondary pump) to compressor - PFIRE E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) compared to: tank (secondary pump) to compressor - PFIRE F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - A07_B05_C04_tank to compressor DISCHARGE - release) Parameters

Inputs

tank (secondary pump) to compressor - PFIRE D3 (linked to Liquefied Gas Bottom Discharge

(TPDIS model) - A07_B05_C04_tank to

compressor DISCHARGE - release)


(TPDIS model) -A07_B05_C04_tank to


tank (secondary pump) to compressor - PFIRE E5 (linked to Liquefied Gas Bottom Discharge



tank (secondary pump) to compressor - PFIRE F2 (linked to Liquefied Gas Bottom Discharge








3,6365E07 3,6365E07 3,6365E07 3,6365E07


217,35 217,35 217,35 217,35


1800 1800 1800 1800


1500 1500 1500 1500

Height of the 0 0 0 0



observer position above ground level (m) Height of the confined pool above ground level (m)

0 0 0 0

Hole diameter (mm)

101,6 101,6 101,6 101,6



Pool thickness (mm)


19 19 19 19


3 9 5 2


1000 1000 1000 1000




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4

Results


(TPDIS model) - A07_B05_C04_tank to





tank (secondary pump) to compressor - PFIRE E5 (linked to Liquefied Gas Bottom Discharge



tank (secondary pump) to compressor - PFIRE F2 (linked to Liquefied Gas Bottom Discharge




43,702 43,702 43,702 43,702


0,016398 0,011267 0,013952 0,017793


86,619 83,77 86,47 84,119


76,882 76,756 78,151 73,852




65,297 68,964 68,43 61,726


117 117 117 117


3,1081E05 3,1081E05 3,1081E05 3,1081E05


64,794 74,662 69,177 64,794

Flame tilt (deg) 41,709 56,97 49,28 35,336View factor (%) 0,05588 0,032466 0,044003 0,060632Atmospheric transmissivity (%)

45,291 46,484 45,836 45,291


762,39 799,53 779,37 762,39


50,24 39,95 45,199 50,24


1500 1500 1500 1500


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69



-



B.06 – ONBOARD TANK TO COMPRESSOR SECONDARY PUMP RELEASE Case description: onboard tank to compressor - release Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)Type of release Release from vessel through (a hole in) pipePipeline length (m) 26,5Pipeline diameter (inch) 4Pipeline roughness (mm) 0,045Hole diameter (mm) 101,6Hole rounding Rounded edgesDischarge coefficient (-) 1Height difference between pipe entrance and exit (m) 0Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 35000Vessel type Vertical cylinderHeight cylinder (m) 26,5Filling degree (%) 99Expansion type Adiabaticn value Pressure inside vessel determination Use actual pressureInitial (absolute) pressure in vessel (bar) 28Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 1,4783E07Initial (vapour) pressure in vessel (bar) 28Time needed to empty vessel (s) 6,5782E05Massflowrate at end outflow (kg/s) 0Total mass released (kg) 1,321E07Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -162,87VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 1,5218E06Vapour mass in vessel at end outflow (kg) 51270Height of liquid at end outflow (m) 2,7139Fillingdegree at end outflow (%) 10,241Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -162,87Maximum mass flow rate (kg/s) 222,93Representative release rate (kg/s) 199,99Representative outflow duration (s) 1800Representative temperature (°C) -161Representative pressure at exit (bar) 1,0612Representative vapour mass fraction (%) 0 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




EVAPORATION Case description: onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release) Model: Pool evaporation version: 5.16 (25/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release) compared to: onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release) compared to: onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release) Parameters

Inputs

onboard tank (secondary pump) to

compressor -evaporation D3 (linked

to Liquefied Gas Bottom Discharge

(TPDIS model) -onboard tank to

compressor - release)







compressor -evaporation E5 (linked





compressor -evaporation F2 (linked



compressor - release)Chemical name (DIPPR)










199,99 199,99 199,99 199,99


1800 1800 1800 1800


1,321E07 1,321E07 1,321E07 1,321E07

Height pool at t=0 Value pool height at t=0 (m)





19 19 19 19


10000 10000 10000 10000



19 19 19 19


500 500 500 500


3 9 5 2


19 19 19 19

Ambient relative 75 75 75 75



humidity (%) Solar radiation flux



100 100 100 100

Cloud cover (%) Date: day number Date: month number

Date: year number


Type of subsoil Subsoil roughness description


1800 1800 1800 1800

Results




















compressor - release)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1


104 104 104 104


1074 1074 1074 1074


499,51 499,51 499,51 499,51


720,67 720,67 720,67 720,67


-161,49 -161,49 -161,49 -161,49


31,969 31,969 31,969 31,969


1,7552 1,6609 1,7197 1,7748


3,5998E05 3,5998E05 3,5998E05 3,5998E05


1074 1074 1074 1074

Corresponding representative pool surface area

802,67 802,67 802,67 802,67



(m2) Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


DISPERSION Case description: onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) compared to: onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) compared to: onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) Parameters

Inputs


compressor - dispersion D3 (linked to Pool

evaporation - onboard tank (secondary pump)

to compressor -evaporation D3 (linked



compressor - release))









compressor - dispersion E5 (linked to Pool


to compressor -evaporation E5 (linked





compressor - dispersion F2 (linked to Pool


to compressor -evaporation F2 (linked



compressor - release))Chemical name (DIPPR)






releaseTotal massreleased (kg)

1,321E07 1,321E07 1,321E07 1,321E07


499,51 499,51 499,51 499,51


720,67 720,67 720,67 720,67



802,67 802,67 802,67 802,67



-161,49 -161,49 -161,49 -161,49


0 0 0 0

Y-coordinate of 0 0 0 0



release (m) Z-coordinate (height) of release (m)


19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results
















compressor - dispersion E5 (linked to Pool







compressor - dispersion F2 (linked to Pool





compressor - release))Explosive mass at time t (kg)

0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0

Maximum 25044 16037 16827 57626



explosive mass (kg) ...at time tmem (s)

110 450 650 300


96,482 48,742 63,409 182,26


720,67 720,67 720,67 720,67


110,61 479,58 107,15 175


149,43 59,66 132,57 359,58


-26,218 -19,503 -21,197 -55,415


12920 20723 11134 43905

...at time tmac (s)

720,67 720,67 720,67 720,67


20365 16037 15678 57626


110,61 479,58 107,15 175


149,43 59,66 132,57 359,58


-26,218 -19,503 -21,197 -55,415


29,088 220,29 32,378 32,088


0 0 0,011686 0,04733



EXPLOSION Case description: tank (secondary pump) to compressor - uvce D3 LC1 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))



Model: Explosion (Multi Energy model) version: 5.03 (25/07/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D3 LC10 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D3 LC50 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D9 LC10 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)) compared to: tank (secondary pump) to compressor - uvce D9 LC50 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC10 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC50 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC10 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC50 PNEW (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Parameters

Inputs

tank (second

ary pump)

to compres

sor -uvce D3

LC1 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce D9

LC1 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce E5

LC1 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce F2

LC1 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce D3

LC10 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce D3

LC50 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce D9

LC10 PNEW (linked to Pool

evaporation -

onboard tank

tank (second

ary pump)

to compres

sor -uvce D9

LC50 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce E5

LC10 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce E5

LC50 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce F2

LC10 PNEW (linked

to Dense

Gas Dispersi

on:

tank (second

ary pump)

to compres

sor -uvce F2

LC50 PNEW (linked

to Dense

Gas Dispersi

on:



Explosive mass -onboard

tank (second

ary pump)

to compres

sor -dispersi

on D3 PNEW (linked to Pool

evaporation -

onboard tank

(secondary

pump) to

compressor -

evaporation D3 PNEW (linked

to Liquefie

d Gas Bottom Dischar

ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi

on E5 PNEW (linked to Pool

evaporation -

onboard tank

(secondary

pump) to

compressor -

evaporation E5 PNEW (linked

to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi

on F2 PNEW (linked to Pool

evaporation -

onboard tank

(secondary

pump) to

compressor -

evaporation F2 PNEW (linked

to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


tank (second

ary pump)

to compres

sor -dispersi


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)

METHANE

(DIPPR)Ambient pressure (bar)

1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


22341 17878 18047 66077 22341 22341 17878 17878 18047 18047 66077 66077


8 8 8 8 8 8 8 8 8 8 8 8

Curve number

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra

3 (Weak deflagra



tion) tion) tion) tion) tion) tion) tion) tion) tion) tion) tion) tion)Distance from release (Xd) (m)

50 50 50 50 50 50 50 50 50 50 50 50


429,91 -9,8282 33,214 33,547 429,91 429,91 -9,8282 -9,8282 33,214 33,214 33,547 33,547


168 168 168 168 365 942 365 942 365 942 365 942


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0


N N N N N N N N N N N N


0 0 0 0 0 0 0 0 0 0 0 0

Results

tank (second

ary pump)

to compres

sor -uvce D3

LC1 PNEW (linked

to Dense

Gas Dispersi

on: Explosive mass -onboard

tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce D9

LC1 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce E5

LC1 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce F2

LC1 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce D3

LC10 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce D3

LC50 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce D9

LC10 PNEW (linked to Pool

evaporation -

onboard tank

(secondary

pump) to

compressor -

evaporation D9

tank (second

ary pump)

to compres

sor -uvce D9

LC50 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce E5

LC10 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce E5

LC50 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce F2

LC10 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to

tank (second

ary pump)

to compres

sor -uvce F2

LC50 PNEW (linked

to Dense

Gas Dispersi


tank (second

ary pump)

to



compressor -

dispersion D3

PNEW (linked to Pool

evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion D9


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion E5


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion F2


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion D3


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion D3


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

PNEW (linked

to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW))

compressor -

dispersion D9


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion E5


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion E5


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion F2


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))

compressor -

dispersion F2


evaporation -

onboard tank

(secondary

pump) to

compressor -


to Liquefie


ge (TPDIS

model) -onboard

tank to compres

sor -release

PNEW)))


1787,3 1430,2 1443,8 5286,1 1787,3 1787,3 1430,2 1430,2 1443,8 1443,8 5286,1 5286,1


89419 71556 722332,6447E

0589419 89419 71556 71556 72233 72233

2,6447E05

2,6447E05


52,382 51,686 51,768 52,785 52,382 52,382 51,686 51,686 51,768 51,768 52,785 52,785


10,292 8,285 8,3541 21,429 10,292 10,292 8,285 8,285 8,3541 8,3541 21,429 21,429


1511,1 1371,9 1378,3 2443,1 1511,1 1511,1 1371,9 1371,9 1378,3 1378,3 2443,1 2443,1

Positive phase duration

576,93 530,85 532,51 925,68 576,93 576,93 530,85 530,85 532,51 532,51 925,68 925,68



at Xd (ms) Dist. from center mass of cloud at threshold overpressure (m)

-1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave


Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).

Minor damage

(Zone D: 3.5 -

17 kPa).


Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).

Habitable after

relatively easy

repairs. Minor

structural

damage (3 kPa).



damage


damage


damage


damage


damage


damage


damage


damage


damage


damage


damage


damage



damage


damage


damage


damage


damage


damage


damage


damage


damage


damage


damage


damage



POOL FIRE Case description: onboard tank (secondary pump) to compressor - PFIRE D3 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) Model: Pool fire version: 5.11 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: onboard tank (secondary pump) to compressor - PFIRE D9 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) compared to: onboard tank (secondary pump) to compressor - PFIRE E5 (linked to Pool evaporation - onboard



tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) compared to: onboard tank (secondary pump) to compressor - PFIRE F2 (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release)) Parameters

Inputs


compressor - PFIRE D3 (linked to Pool



to Liquefied Gas Bottom Discharge (TPDIS

model) - onboard tank to compressor -

release))







release))


compressor - PFIRE E5 (linked to Pool





release))


compressor - PFIRE F2 (linked to Pool





release))Chemical name (DIPPR)





1,321E07 1,321E07 1,321E07 1,321E07


499,51 499,51 499,51 499,51


720,67 720,67 720,67 720,67


10000 10000 10000 10000


0 0 0 0


0 0 0 0

Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate



Fraction combustion

35 35 35 35



heat radiated (%) Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of soot fraction (-)


3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4


Results



evaporation - onboard





compressor - PFIRE E5 (linked to Pool



compressor - PFIRE F2 (linked to Pool






Discharge (TPDIS model) - onboard tank

to compressor -release))














112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194


198,96 193,87 200,39 195,03


177,63 177,35 181,02 172,64


153,44 159,19 159,19 147,33


780 780 780 780


16936 16936 16936 16936


78,846 87,066 80,77 78,846


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69

Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010



Chemical source date 14/09/2010




B.07– PIPELINE FROM SECONDARY PUMP TO RU RELEASE Case description: B07_pump to ru - release Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (07/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)Type of release Release from vessel through (a hole in) pipePipeline length (m) 26,5Pipeline diameter (inch) 6Pipeline roughness (mm) 0,045Hole diameter (m) 0,1524Hole rounding Rounded edgesDischarge coefficient (-) 1Height difference between pipe entrance and exit (m) 0Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 90000Vessel type Horizontal cylinderLength cylinder (m) 26,5Filling degree (%) 99Expansion type Adiabaticn value Pressure inside vessel determination Use actual pressureInitial (absolute) pressure in vessel (bar) 28Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 3,8014E07Initial (vapour) pressure in vessel (bar) 28Time needed to empty vessel (s) 4,2649E05Massflowrate at end outflow (kg/s) 0Total mass released (kg) 3,6387E07Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -164,42VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 1,503E06Vapour mass in vessel at end outflow (kg) 1,2479E05Height of liquid at end outflow (m) 5,4165Fillingdegree at end outflow (%) 3,9125Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -164,42Maximum mass flow rate (kg/s) 600,89Representative release rate (kg/s) 539,25Representative outflow duration (s) 1800Representative temperature (°C) -161Representative pressure at exit (bar) 1,0643Representative vapour mass fraction (%) 0 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




EVAPORATION Case description: B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Model: Pool evaporation version: 5.16 (20/06/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) compared to: B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) compared to: B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Parameters

Inputs

B07_pump to RU -evaporation D3 (linked


(TPDIS model) -B07_pump to ru -

release)




release)

B07_pump to RU -evaporation E5 (linked



release)

B07_pump to RU -evaporation F2 (linked



release)Chemical name (DIPPR)








Land Land Land Land


539,25 539,25 539,25 539,25


1800 1800 1800 1800


3,6387E07 3,6387E07 3,6387E07 3,6387E07






19 19 19 19


1500 1500 1500 1500


19 19 19 19




3 9 5 2


19 19 19 19


75 75 75 75

Solar radiation flux User defined User defined User defined User definedSolar heat radiation flux (W/m2)

100 100 100 100

Cloud cover (%)



Date: day number Date: month number

Date: year number Latitude of the location (deg)

Type of subsoil Heavy concrete Heavy concrete Heavy concrete Heavy concrete


flat sandy soil, concrete, tiles, plant-

yard


yard


yard


yardMaximum evaluation time for evaporation (s)

1800 1800 1800 1800

Results




release)




release)




release)

B07_pump to RU -evaporation F2 (linked



release)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1


34,5 34,5 34,5 34,5



52,281 62,311 51,892 53,861


1068,6 1449,8 1350,9 882,95


-161,49 -161,49 -161,49 -161,49


29,033 31,883 28,512 29,892


1,5121 1,369 1,4372 1,5733


55867 90337 70102 47556


1799,5 1799,5 1799,5 1799,5


662,01 798,37 638,49 701,78





ATMOSPHERIC DISPERSION Case description: B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (20/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) compared to: B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) compared to: B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) Parameters

Inputs

B07_pump to ru - dispersion D3 (linked to

Pool evaporation - B07_pump to RU -

evaporation D3 (linked to Liquefied Gas


B07_pump to ru - release))

B07_pump to ru -dispersion D9 (linked to

Pool evaporation -B07_pump to RU -



B07_pump to ru -release))

B07_pump to ru -dispersion E5 (linked to


evaporation E5 (linked to Liquefied Gas



B07_pump to ru -dispersion F2 (linked to


evaporation F2 (linked to Liquefied Gas









releaseTotal mass released (kg)

3,6387E07 3,6387E07 3,6387E07 3,6387E07


52,281 62,311 51,892 53,861


1068,6 1449,8 1350,9 882,95



662,01 798,37 638,49 701,78



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data



D (Neutral) D (Neutral) D (Neutral) D (Neutral)


3 9 5 2



N N N N

Wind comes from 0 0 0 0



(North = 0 degrees) (deg) Ambient relative humidity (%)

75 75 75 75




1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results

B07_pump to ru - dispersion D3 (linked to

Pool evaporation - B07_pump to RU -



B07_pump to ru - release))

B07_pump to ru -dispersion D9 (linked to





B07_pump to ru -dispersion E5 (linked to





B07_pump to ru -dispersion F2 (linked to






0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


1834,7 190,3 669,32 4050,5


95 95 95 165,8


1068,6 1449,8 1350,9 882,95


191,4 72,008 120,8 261,48


42,652 33,238 37,665 46,537


-16,92 -16,21 -15,976 -17,729

Maximum area of explosive cloud

5968,9 1885,1 3410,2 9829,6



(m2) ...at time tmac (s) 1068,6 1449,8 1350,9 882,95Explosive mass at time tmac (kg)

1834,7 190,3 669,32 4050,5


191,4 16,206 120,8 261,48


42,652 30,5 37,665 46,537


-16,92 -16,21 -15,976 -17,729


78,783 -8,1074 44,423 113,01


0 0 0 0



EXPLOSION Case description: B07_pump to ru - uvce D3 LC1 copy (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Model: Explosion (Multi Energy model) version: 5.03 (07/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B07_pump to ru - uvce D9 LC1 copy (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 LC1 copy (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce F2 LC1 copy (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Parameters

Inputs

B07_pump to ru - uvce D3 LC1 copy (linked to Dense Gas Dispersion:

Explosive mass - B07_pump to ru -

dispersion D3 (linked to Pool evaporation - B07_pump to RU -



B07_pump to ru - release)))


Explosive mass -B07_pump to ru -

dispersion D9 (linked to Pool evaporation -B07_pump to RU -



B07_pump to ru -release)))

B07_pump to ru - uvce E5 LC1 copy (linked to Dense Gas Dispersion:


dispersion E5 (linked to Pool evaporation -B07_pump to RU -


Discharge (TPDIS model) - B07_pump to

ru - release)))

B07_pump to ru - uvce F2 LC1 copy (linked to Dense Gas Dispersion: Explosive

mass - B07_pump to ru -dispersion F2 (linked to



Discharge (TPDIS model) - B07_pump to ru -

release)))






1,0151 1,0151 1,0151 1,0151


1834,7 190,3 669,32 4050,5


8 8 8 8

Curve number 5 (Medium

deflagration) 5 (Medium

deflagration)5 (Medium deflagration) 5 (Medium deflagration)


50 50 50 50


78,783 -8,1074 44,423 113,01


100 100 100 100


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results


Explosive mass - B07_pump to ru -

dispersion D3 (linked to Pool evaporation - B07_pump to RU -



B07_pump to ru - release)))



dispersion D9 (linked to Pool evaporation -B07_pump to RU -



B07_pump to ru -release)))

B07_pump to ru - uvce E5 LC1 copy (linked to Dense Gas Dispersion:


dispersion E5 (linked to Pool evaporation -B07_pump to RU -



ru - release)))

B07_pump to ru - uvce F2 LC1 copy (linked to Dense Gas Dispersion: Explosive

mass - B07_pump to ru -dispersion F2 (linked to



Discharge (TPDIS model) - B07_pump to ru -

release)))


146,77 15,224 53,546 324,04


7343,2 761,68 2679 16212


101,67 48,747 73,026 132,22


9,2877 1,4994 4,1851 17,037


429,45 100,16 223,17 717,99




84,475 41,096 61,121 108,6


50,843 23,889 36,329 66,204

















failed, serious damage to the remaining

carrying elements. Damage to



Minor damage. Comparable to a damage due to a

storm; wooden walls fail, breakage of

windows (7-10 kPa).










ondulated plates have failed 7-14 kPa). The roof of a storage tank

has collapsed (7 kPa).











POOL FIRE Case description: B07_pump to RU - PFIRE D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Model: Pool fire version: 5.11 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B07_pump to RU - PFIRE D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) compared to: B07_pump to RU - PFIRE E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) compared to: B07_pump to RU - PFIRE F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Parameters Inputs B07_pump to RU - B07_pump to RU - B07_pump to RU - B07_pump to RU -



PFIRE D3 (linked to Liquefied Gas Bottom


ru - release)

PFIRE D9 (linked to Liquefied Gas Bottom


ru - release)

PFIRE E5 (linked to Liquefied Gas Bottom


ru - release)

PFIRE F2 (linked toLiquefied Gas Bottom


ru - release)Chemical name (DIPPR)





3,6387E07 3,6387E07 3,6387E07 3,6387E07


539,25 539,25 539,25 539,25


1800 1800 1800 1800


1500 1500 1500 1500


0 0 0 0


0 0 0 0

Hole diameter (mm)

152,4 152,4 152,4 152,4


1 1 1 1



Pool thickness (mm)


19 19 19 19

Pool burning rate Calculate/Default Calculate/Default Calculate/Default Calculate/DefaultValue of pool burning rate (kg/m2*s)


35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000

Exposure 75 75 75 75



duration to heat radiation (s) Take protective effects of clothing into account

No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4


Results

B07_pump to RU -PFIRE D3 (linked to

Liquefied Gas Bottom Discharge (TPDIS

model) - B07_pump to ru - release)

B07_pump to RU -PFIRE D9 (linked to



B07_pump to RU -PFIRE E5 (linked to



B07_pump to RU -PFIRE F2 (linked to




43,702 43,702 43,702 43,702


0,016398 0,011267 0,013952 0,017793


86,619 83,77 86,47 84,119


76,882 76,756 78,151 73,852


65,297 68,964 68,43 61,726


117 117 117 117


3,11E05 3,11E05 3,11E05 3,11E05


64,794 74,662 69,177 64,794

Flame tilt (deg) 41,709 56,97 49,28 35,336View factor (%) 0,05588 0,032466 0,044003 0,060632Atmospheric 45,291 46,484 45,836 45,291



transmissivity (%) Flame temperature (°C)

762,39 799,53 779,37 762,39


50,24 39,95 45,199 50,24


1500 1500 1500 1500


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69





B.08 – REGASIFICATION UNIT JET FIRE Case description: B08_vaporizer - JFIRE D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (07/11/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B08_vaporizer - JFIRE D9 compared to: B08_vaporizer - JFIRE E5 compared to: B08_vaporizer - JFIRE F2 Parameters

Inputs B08_vaporizer -

JFIRE D3B08_vaporizer -


JFIRE E5B08_vaporizer -

JFIRE F2Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Type of release Release through

hole in vesselRelease through



hole in vesselPipeline length (m) Pipeline diameter (mm) Pipeline roughness (mm) Hole diameter (inch) 1,5 1,5 1,5 1,5Hole rounding Rounded edges Rounded edges Rounded edges Rounded edgesDischarge coefficient (-) 1 1 1 1Initial temperature in vessel (°C)

-150 -150 -150 -150


25 25 25 25


0 0 0 0


1 1 1 1


3 9 5 2

Ambient temperature (°C) 19 19 19 19Ambient relative humidity (%) 75 75 75 75Flame temperature (K) 1500 1500 1500 1500Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0

Distance from release (Xd) (m) 100 100 100 100X-coordinate of release (m) 0 0 0 0Y-coordinate of release (m) 0 0 0 0Predefined wind direction N N N NWind comes from (North = 0 degrees) (deg)

0 0 0 0

Results B08_vaporizer -



JFIRE E5B08_vaporizer -

JFIRE F2Initial source strength (kg/s) 12,828 12,828 12,828 12,828Type of flow of the jet Choked flow Choked flow Choked flow Choked flowExit velocity of expanding jet (m/s)

530,59 530,59 530,59 530,59


0 0 0 0


0,090821 0,085632 0,0887 0,095981

Width of frustum tip (W2) (m) 13,117 11,94 12,074 14,184Length of frustum (flame) (Rl) (m)

36,289 28,414 31,52 40,549

Tilt angle central axis flare 0 0 0 0



(alpha_b) (deg) Surface area of frustum (m2) 900,04 660,25 727,49 1081,2Surface area of a cylinder (m2) 821,38 593,51 660,3 989,61Surface emissive power (max) (kW/m2)

115,52 159,87 143,7 95,88


115,52 159,87 143,7 95,88

Atmospheric transmissivity (%) 74,567 74,433 74,48 74,656View factor (%) 0,36387 0,21689 0,25114 0,52133Heat radiation at Xd (kW/m2) 0,32463 0,26465 0,27672 0,38865 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


ATMOSPHERIC DISPERSION Case description: B08_vaporizer - dispersion D3 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (07/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B08_vaporizer - dispersion D9 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3) compared to: B08_vaporizer - dispersion E5 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3) compared to: B08_vaporizer - dispersion F2 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3) Parameters

Inputs

B08_vaporizer -dispersion D3 (linked

to Gas Jet Fire (Chamberlain model) -B08_vaporizer - JFIRE

D3)



D3)

B08_vaporizer -dispersion E5 (linked


D3)

B08_vaporizer -dispersion F2 (linked to

Gas Jet Fire (Chamberlain model) -B08_vaporizer - JFIRE

D3)Chemical name (DIPPR)


Type of release Semi-continuous Semi-continuous Semi-continuous Semi-continuousTotal mass released (kg)


1848 1848 1848 1848


120 120 120 120


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0

Length source in vertical (z) direction

0 0 0 0



(m) Ambient temperature (°C)

19 19 19 19

Meteorological data Pasquill Pasquill Pasquill PasquillPasquill stability class



3 9 5 2


35 35 35 35





High crops; scattered large objects, 15 < x/h

< 20.


< 20.


< 20.


< 20.Predefined wind direction

N N N N


0 0 0 0


120 120 120 120


20 20 20 20


0,1 0,1 0,1 0,1


Low Low Low Low

Results



D3)



D3)

B08_vaporizer -dispersion E5 (linked


D3)

B08_vaporizer -dispersion F2 (linked to


D3)Total explosive mass at time t (kg)

1,2366E05 1,331E05 1,4426E05 39379


48,6 46,8 39,6 28,3


430,29 1018,1 698,5 302,86


70,686 70,246 69,776 53,239


0,01 0,01 0,01 0,01


1,9709E05 1,3462E05 1,8376E05 2,0106E05

...at time tmem (s) 200 125 200 500




184,31 113,2 144,42 472,29


233,44 130,67 220,57 604,67

Length of cloud (between LEL) at end of release (m)

430,29 1018,1 698,5 302,86

Width of cloud (between LEL) at end of release (m)

70,686 70,246 69,776 53,239

Offset between release location and LEL at end of release (m)

0,01 0,01 0,01 0,01


48651 56924 66800 83225

...at time tmac (s) 350 125 300 1250Explosive mass at time tmac (kg)

1,4349E05 1,3462E05 1,3483E05 1,0407E05


557,96 1014 814,8 941,29


110,2 70,337 102,2 114,06


574,35 33,235 760,48 1891


853,33 540,24 1167,9 2361,6


0 0 0,014548 0,060302


500 500 247,92 62,735


0,63265 1,8979 0,88561 0,23504


0,43475 1,3042 0,60594 0,16082



EXPLOSION



Case description: B08_vaporizer - uvce D3 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B08_vaporizer - dispersion D3 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3)) Model: Explosion (Multi Energy model) version: 5.03 (07/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B08_vaporizer - uvce D9 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B08_vaporizer - dispersion D9 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3)) compared to: B08_vaporizer - uvce E5 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B08_vaporizer - dispersion E5 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3)) compared to: B08_vaporizer - uvce F2 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B08_vaporizer - dispersion F2 (linked to Gas Jet Fire (Chamberlain model) - B08_vaporizer - JFIRE D3)) Parameters

Inputs

B08_vaporizer - uvce D3 LC1 (linked to Neutral

Gas Dispersion: Explosive mass -B08_vaporizer -

dispersion D3 (linked to Gas Jet Fire

(Chamberlain model) -B08_vaporizer - JFIRE

D3))





D3))

B08_vaporizer - uvce E5 LC1 (linked to Neutral


dispersion E5 (linked to Gas Jet Fire


D3))

B08_vaporizer -uvce F2 LC1 (linked

to Neutral Gas Dispersion:

Explosive mass -B08_vaporizer -

dispersion F2 (linked to Gas Jet Fire

(Chamberlain model) - B08_vaporizer -

JFIRE D3))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


1,4349E05 1,3462E05 1,3483E05 1,0407E05


8 8 8 8

Curve number 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration)5 (Medium

deflagration)Distance from release (Xd) (m)

50 50 100 100


853,33 540,24 1167,9 2361,6


100 100 100 100


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results


Gas Dispersion: Explosive mass -



B08_vaporizer - uvce E5 LC1 (linked to Neutral


B08_vaporizer -uvce F2 LC1 (linked




B08_vaporizer -dispersion D3 (linked to


D3))

B08_vaporizer -dispersion D9 (linked to


D3))

B08_vaporizer -dispersion E5 (linked to


D3))

Explosive mass -B08_vaporizer -


(Chamberlain model) - B08_vaporizer -

JFIRE D3))Confined mass in explosive range (kg)

11480 10770 10786 8325,5


5,7433E05 5,3882E05 5,3964E05 4,1654E05


206,07 206,07 200,13 190,92


92,932 92,932 51,604 42,521


4825,6 4687,8 3501,3 3030,6


468,36 454,98 349,9 317,47


217,43 212,86 212,96 195,35








kPa).
















damage to the remaining carrying elements. Damage

to windowframes and doors (7-15

kPa).












walls and doors; failure of joints.

Doors and window frames have failed. Wall covering has

fallen down (15 kPa).


Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-

framing structure


framing structure


framing structure


have collapsed (15-20). Minor damage to steel frames (8-



collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30

kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have

fallen down (20-40 kPa). Walls made of concrete

blocks have collapsed (15-20). Minor damage to

steel frames (8-10 kPa). Connections between

steel or aluminium ondulated plates have

failed 7-14 kPa). The roof of a storage tank has

collapsed (7 kPa).








collapsed (7 kPa).








collapsed (7 kPa).

10 kPa). Connections




collapsed (7 kPa).



DISPERSION Case description: B09_RU to ME - dispersion D3 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (21/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B09_RU to ME - dispersion D9 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3) compared to: B09_RU to ME - dispersion E5 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3) compared to: B09_RU to ME - dispersion F2 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3) Parameters

Inputs

B09_RU to ME -dispersion D3 (linked

to Gas Jet Fire (Chamberlain model) -

B09_RU to ME - JFIRE D3)




B09_RU to ME -dispersion E5 (linked



B09_RU to ME -dispersion F2 (linked


B09_RU to ME -JFIRE D3)



Type of release Semi-continuous Semi-continuous Semi-continuous Semi-continuousTotal mass released (kg)


188,45 188,45 188,45 188,45


120 120 120 120


0 0 0 0


0 0 0 0


0 0 0 0

Length source in 0 0 0 0



wind (x) direction (m) Length source in crosswind (y) direction (m)

0 0 0 0


0 0 0 0


19 19 19 19

Meteorological data Pasquill Pasquill Pasquill PasquillPasquill stability class

D (Neutral) D (Neutral) E (Stable) D (Neutral)


3 9 5 3


51 51 51 51






< 20.


< 20.


< 20.



N N N N


0 0 0 0


120 120 120 120


20 20 20 20


0,1 0,1 0,1 0,1


Low Low Low Low

Results







B09_RU to ME -dispersion E5 (linked



B09_RU to ME -dispersion F2 (linked


B09_RU to ME -JFIRE D3)


15626 3783,7 13761 15626


26,9 16,8 19,3 26,9


369,24 323,28 568,8 369,24


34,845 19,997 31,318 34,845




0,01 0,01 0,01 0,01


16063 3783,7 13873 16063


117,17 36,262 113,26 117,17


141,58 121,29 130,83 141,58


369,24 323,28 568,8 369,24


34,845 19,997 31,318 34,845


0,01 0,01 0,01 0,01


11104 5050,6 14244 11104


11938 3783,7 10900 11938


357,77 323,28 537,6 357,77


36,574 19,997 31,456 36,574


136,86 0,01 120,83 136,86


315,75 161,65 389,63 315,75


0 0 0,014548 0


500 500 212,99 500


0,63265 1,8979 0,88561 0,63265


0,43475 1,3042 0,60594 0,43475






EXPLOSION Case description: B09_RU to ME - UVCE D3 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3)) Model: Explosion (Multi Energy model) version: 5.03 (25/06/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B09_RU to ME - UVCE D9 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3)) compared to: B09_RU to ME - UVCE E5 LC1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3)) compared to: B09_RU to ME - UVCE F2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3)) Parameters

Inputs

B09_RU to ME - UVCE D3 LC1 (linked to

Neutral Gas Dispersion: Explosive mass -B09_RU to ME -


(Chamberlain model) -B09_RU to ME - JFIRE

D3))





D3))

B09_RU to ME - UVCE E5 LC1 (linked to




D3))

B09_RU to ME - UVCE F2 (linked to Neutral

Gas Dispersion: Explosive mass -B09_RU to ME -



D3))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


11938 3783,7 10900 11938


8 8 8 8

Curve number 3 (Weak deflagration) 3 (Weak deflagration) 3 (Weak deflagration) 3 (Weak deflagration)Distance from release (Xd) (m)

50 50 100 50


315,75 161,65 389,63 315,75


168 168 168 300


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results B09_RU to ME - UVCE

D3 LC1 (linked to Neutral Gas Dispersion:


Neutral Gas Dispersion:

B09_RU to ME - UVCE E5 LC1 (linked to

Neutral Gas Dispersion:

B09_RU to ME - UVCE F2 (linked to Neutral

Gas Dispersion:



Explosive mass -B09_RU to ME -



D3))




D3))




D3))




D3))Confined mass in explosive range (kg)

955,04 302,7 871,96 955,04


47782 15144 43625 47782


48,306 35,4 24,944 48,306


5,6992 1,9672 1,0151 5,6992


1120,7 559,94 561,39 1120,7


463,99 316,35 450,12 463,99


-1E100 -1E100 -1E100 -1E100













Damage to roofs, ceilings, minor crack

formation in plastering, more than

1% damage to glass panels (1 - 1.5 kPa)

















B.10 - PIPELINE FROM FSU TANK TO COMPRESSOR RELEASE Case description: B10_tank to BOC - release Model: Gas Release From Vessel version: 5.09 (20/06/2013) Reference: Yellow Book, CPR-14E, 3rd edition 1997, Paragraph 2.5.2.3 and Yellow Book, CPR-14E, 3rd edition 1997, Paragraph 2.5.2.3 Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)Expansion type Adiabaticn value Type of release Release from vessel through (a hole in) pipePipeline length (m) 53Pipeline diameter (inch) 6Pipeline roughness (mm) 0,045Hole diameter (inch) 6Hole rounding Sharp edgesDischarge coefficient (-) 0,62Initial temperature in equipment (°C) -150Initial (absolute) pressure in vessel (bar) 1,1Vessel volume (m3) 20Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 35,483Mass flow rate at time t (kg/s) Time needed to empty vessel (s) 3,8144Total mass released (kg) 2,0656Pressure in vessel at time t (bar) Pressure at pipe exit at time t (bar) Temperature at pipe exit at time t (°C) Density gas at pipe exit at time t (kg/m3) Maximum mass flow rate (kg/s) 1,1052Representative release rate (kg/s) 1,0448Representative outflow duration (s) 1,977Representative temperature (°C) -150,25Representative pressure (bar) 1,0409Representative density (kg/m3) 1,6798 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


JET FIRE Case description: B10_tank to BOC - JFIRE D3 not realistic copy Model: Gas Jet Fire (Chamberlain model) version: 5.12 (17/10/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)



Type of release Release from vessel through (a hole in) pipePipeline length (m) 25000Pipeline diameter (inch) 6Pipeline roughness (mm) 0,045Hole diameter (inch) 6Hole rounding Rounded edgesDischarge coefficient (-) 1Initial temperature in vessel (°C) 19Initial (absolute) pressure in vessel (bar) 38Outflow angle in XZ plane (0°=horizontal; 90°=vertical) (deg) 0Release height (Stack height) (m) 40Wind speed at 10 m height (m/s) 3Ambient temperature (°C) 19Ambient relative humidity (%) 75Flame temperature (°C) 1500Amount of CO2 in atmosphere (%) 0,03Percentage of the flame covered by soot (%) 0Distance from release (Xd) (m) 100X-coordinate of release (m) 0Y-coordinate of release (m) 0Predefined wind direction NWind comes from (North = 0 degrees) (deg) 0

Results Initial source strength (kg/s) 3,9424Type of flow of the jet Choked flowExit velocity of expanding jet (m/s) 859,76Angle between hole and flame axis (alpha) (deg) 0,53242Frustum lift off height (b) (m) 4,5221Width of frustum base (W1) (m) 0,060633Width of frustum tip (W2) (m) 6,7133Length of frustum (flame) (Rl) (m) 19,592Tilt angle central axis flare (alpha_b) (deg) 0,43257Surface area of frustum (m2) 246,85Surface area of a cylinder (m2) 226,48Surface emissive power (max) (kW/m2) 107,18Surface emissive power (actual) (kW/m2) 107,18Atmospheric transmissivity (%) 78,312View factor (%) 0,13592Heat radiation at Xd (kW/m2) 0,11437 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


B.11 – COMPRESSOR RELEASE Case description: B11_tank to BOC - release Model: Gas Release From Vessel version: 5.09 (20/06/2013) Reference: Yellow Book, CPR-14E, 3rd edition 1997, Paragraph 2.5.2.3 and Yellow Book, CPR-14E, 3rd edition 1997, Paragraph 2.5.2.3 Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Use which representative step First 20% average (flammable)



Expansion type Adiabaticn value Type of release Release from vessel through (a hole in) pipePipeline length (m) 53Pipeline diameter (inch) 6Pipeline roughness (mm) 0,045Hole diameter (inch) 6Hole rounding Sharp edgesDischarge coefficient (-) 0,62Initial temperature in equipment (°C) -150Initial (absolute) pressure in vessel (bar) 1,1Vessel volume (m3) 20Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 35,483Mass flow rate at time t (kg/s) Time needed to empty vessel (s) 3,8144Total mass released (kg) 2,0656Pressure in vessel at time t (bar) Pressure at pipe exit at time t (bar) Temperature at pipe exit at time t (°C) Density gas at pipe exit at time t (kg/m3) Maximum mass flow rate (kg/s) 1,1052Representative release rate (kg/s) 1,0448Representative outflow duration (s) 1,977Representative temperature (°C) -150,25Representative pressure (bar) 1,0409Representative density (kg/m3) 1,6798 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


JET FIRE Case description: B11_tank to BOC - JFIRE D3 not realistic Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/06/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B11_tank to BOC - JFIRE D9 not realistic compared to: B11_tank to BOC - JFIRE E5 not realistic compared to: B11_tank to BOC - JFIRE F2 not realistic Parameters

Inputs B11_tank to BOC -

JFIRE D3 not realistic

B11_tank to BOC - JFIRE D9 not

realistic

B11_tank to BOC -JFIRE E5 not

realistic

B11_tank to BOC -JFIRE F2 not

realisticChemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)




pipe


pipe


pipePipeline length (m) 25000 25000 25000 25000Pipeline diameter (inch) 6 6 6 6Pipeline roughness (mm) 0,045 0,045 0,045 0,045Hole diameter (inch) 6 6 6 6Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges



Discharge coefficient (-) 1 1 1 1Initial temperature in vessel (°C)

19 19 19 19


15 15 15 15


0 0 0 0


40 40 40 40


3 9 5 2


75 75 75 75

Flame temperature (°C) 1500 1500 1500 1500Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03

Percentage of the flamecovered by soot (%)

0 0 0 0


100 100 100 100

X-coordinate of release (m) 0 0 0 0Y-coordinate of release (m) 0 0 0 0Predefined wind direction N N N NWind comes from (North = 0 degrees) (deg)

0 0 0 0

Results B11_tank to BOC -

JFIRE D3 not realistic

B11_tank to BOC - JFIRE D9 not

realistic

B11_tank to BOC -JFIRE E5 not

realistic

B11_tank to BOC -JFIRE F2 not

realisticInitial source strength (kg/s) 1,4993 1,4993 1,4993 1,4993Type of flow of the jet Choked flow Choked flow Choked flow Choked flowExit velocity of expanding jet (m/s)

777,61 777,61 777,61 777,61


1,1355 5,7196 2,3395 0,66464


0,043405 0,041467 0,042632 0,047204


4,4851 3,9538 4,0705 4,8931


13,022 10,508 11,431 14,471


0,924 4,7943 1,9238 0,53788


109,77 79,355 88,005 132,66


100,68 72,212 80,496 121,88


94,649 131,97 118,38 78,188


94,649 131,97 118,38 78,188


78,093 78,044 78,065 78,118


0,03786 0,031165 0,035345 0,039616

Other information Main program Effects 8.1.8.6673Chemical database DIPPR database



Chemical source DIPPR Jan2010Chemical source date 14/09/2010




B.12 - PIPELINE FROM FSU BOC TO FSU LIQUIFIER – DISCHARGE JET FIRE Case description: B12_BOC to Liquifier -not realistic Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/06/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B12_BOC to Liquifier - modified not realistic D3 compared to: B12_BOC to Liquifier - modified not realistic D9 compared to: B12_BOC to Liquifier - modified not realistic E5 compared to: B12_BOC to Liquifier - modified not realistic F2 Parameters

Inputs B12_BOC to Liquifier -not

realistic

B12_BOC to Liquifier -

modified not realistic D3




modified not realistic E5


modified not realistic F2


METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

Type of release Release from

vessel through (a hole in) pipe

Release from vessel through (a

hole in) pipe


hole in) pipe


hole in) pipe


hole in) pipePipeline length (m) 26,5 25000 25000 25000 25000Pipeline diameter (inch)

6 6 6 6 6

Pipeline roughness (mm)

0,045 0,045 0,045 0,045 0,045

Hole diameter (inch) 6 6 6 6 6Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges Rounded edgesDischarge coefficient (-)

1 1 1 1 1

Initial temperature in vessel (°C)

19 19 19 19 19


15 15 15 15 15


0 0 0 0 0


40 40 40 40 40


3 3 9 5 2


19 19 19 19 19


75 75 75 75 75


1500 1500 1500 1500 1500


0,03 0,03 0,03 0,03 0,03


0 0 0 0 0


100 100 100 100 100


0 0 0 0 0


0 0 0 0 0


N N N N N


0 0 0 0 0



Results B12_BOC to Liquifier -not

realistic






modified not realistic E5


modified not realistic F2

Initial source strength (kg/s)

33,485 1,4993 1,4993 1,4993 1,4993

Type of flow of the jet Choked flow Choked flow Choked flow Choked flow Choked flowExit velocity of expanding jet (m/s)

777,61 777,61 777,61 777,61 777,61


0 1,1355 5,7196 2,3395 0,66464

Frustum lift off height (b) (m)

12,808 2,9808 2,0302 2,4702 3,4104

Width of frustum base (W1) (m)

0,20764 0,043405 0,041467 0,042632 0,047204


17,949 4,4851 3,9538 4,0705 4,8931


51,231 13,022 10,508 11,431 14,471


0 0,924 4,7943 1,9238 0,53788


1735,9 109,77 79,355 88,005 132,66


1590,6 100,68 72,212 80,496 121,88


133,8 94,649 131,97 118,38 78,188


133,8 94,649 131,97 118,38 78,188


78,803 78,093 78,044 78,065 78,118

View factor (%) 2,3508 0,051111 0,030187 0,038164 0,064714Heat radiation at Xd (kW/m2)

2,4938 0,03786 0,031165 0,035345 0,039616



DISPERSION Case description: B12_BOC to Liquifier - modified not realistic DISPERSION D3 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B12_BOC to Liquifier - modified not realistic DISPERSION D9 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) compared to: B12_BOC to Liquifier - modified not realistic DISPERSION E5 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) compared to: B12_BOC to Liquifier - modified not realistic DISPERSION F2 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) Parameters

Inputs

B12_BOC to Liquifier -modified not realistic

DISPERSION D3 (linked to Gas Jet Fire


DISPERSION D9 (linked to Gas Jet Fire


DISPERSION E5 (linked to Gas Jet Fire


DISPERSION F2 (linked to Gas Jet Fire



(Chamberlain model) -B12_BOC to Liquifier -

modified not realistic D3)











1,4993 1,4993 1,4993 1,4993



0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


19 19 19 19

Meteorological data





3 9 5 2


51 51 51 51






< 20.


< 20.


< 20.



N N N N


0 0 0 0



20 20 20 20




0,1 0,1 0,1 0,1


Results


DISPERSION D3 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -



DISPERSION D9 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -



DISPERSION E5 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -



DISPERSION F2 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -



9,1894 1,555 6,0631 47,811


3,2 2 2,4 3,3


32,44 16,38 35,9 114,1


2,5029 1,351 2,0542 3,7754


0,01 0,01 0,01 0,01


9,1894 1,555 6,0631 47,811


0 0 0 0


0 0 0 0


32,44 16,38 35,9 114,1


2,5029 1,351 2,0542 3,7754


0,01 0,01 0,01 0,01


64,445 17,673 58,213 336,1


9,1894 1,555 6,0631 47,811


32,44 16,38 35,9 114,1


2,5029 1,351 2,0542 3,7754




0,01 0,01 0,01 0,01


16,23 8,2 17,96 57,06


0 0 0,014548 0,060302


500 500 212,99 53,896


0,63265 1,8979 0,88561 0,23504


0,43475 1,3042 0,60594 0,16082





B.13 - PIPELINE FROM FSU LIQUIFIER TO FSU TANK RELEASE Case description:B13_liquifier to tank - release Model: Liquefied Gas Bottom Discharge (TPDIS model) version: 5.06 (25/07/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 2 and Modelling source terms for the atmospheric dispersion of hazardous substances, Jaakko Kukkonen Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Type of release Release from vessel through (a hole in) pipePipeline length (m) 53Pipeline diameter (inch) 4Hole diameter (m) 0,1016Height difference between pipe entrance and exit (m) 0Height leak above tank bottom (m) 0Initial temperature in vessel (°C) -161Vessel volume (m3) 50Vessel type Horizontal cylinderLength cylinder (m) 53Filling degree (%) 99Pressure inside vessel determination Use actual pressureInitial (absolute) pressure in vessel (bar) 6Type of calculation Calculate until device is emptyTime t after start release (s)

Results Initial mass in vessel (kg) 20885Initial (vapour) pressure in vessel (bar) 6Time needed to empty vessel (s) 3471Massflowrate at end outflow (kg/s) 0Total mass released (kg) 13479Pressure in vessel at end outflow (bar) 1,0151Temperature in vessel at end outflow (°C) -161,67VapourMass fraction at end outflow (%) 100Liquid mass in vessel at end outflow (kg) 7347,3Vapour mass in vessel at end outflow (kg) 58,389Height of liquid at end outflow (m) 0,41548Fillingdegree at end outflow (%) 34,757Exit pressure at end outflow (bar) 1,0151Exit temperature at end outflow (°C) -161,67Maximum mass flow rate (kg/s) 72,37Representative release rate (kg/s) 9,1505Representative outflow duration (s) 1473Representative temperature (°C) -161,32Representative pressure at exit (bar) 1,0268Representative vapour mass fraction (%) 0,096589 Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


POOL EVAPORATION Case description: B13_liquifier to tank - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)



Model: Pool evaporation version: 5.16 (07/11/2013) Reference: Yellow Book CPR14E 2rd Edition - Chapter 5: Evaporation compared to: B13_liquifier to tank - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) Parameters

Inputs

B13_liquifier to tank -evaporation D3 (linked


(TPDIS model) -B13_liquifier to tank -

release)

B13_liquifier to tank - evaporation D9 (linked


(TPDIS model) - B13_liquifier to tank -

release)

B13_liquifier to tank -evaporation E5 (linked



release)

B13_liquifier to tank -evaporation F2 (linked



release)Chemical name (DIPPR)








Land Land Land Land


9,1505 9,1505 9,1505 9,1505


1473 1473 1473 1473


13479 13479 13479 13479






19 19 19 19


2206 2206 2206 2206


19 19 19 19




3 9 5 2


19 19 19 19


75 75 75 75

Solar radiation flux User defined User defined User defined User definedSolar heat radiation flux (W/m2)

100 100 100 100

Cloud cover (%) Date: day number Date: month number



Date: year number Latitude of the location (deg)

Type of subsoil Heavy concrete Heavy concrete Heavy concrete Heavy concrete



yard


yard


yard


yardMaximum evaluation time for evaporation (s)

1800 1800 1800 1800

Results

B13_liquifier to tank -evaporation D3 (linked



release)

B13_liquifier to tank - evaporation D9 (linked


(TPDIS model) - B13_liquifier to tank -

release)

B13_liquifier to tank -evaporation E5 (linked



release)

B13_liquifier to tank -evaporation F2 (linked



release)Heat flux from solar radiation (kW/m2)

0,1 0,1 0,1 0,1




8,6222 8,8372 8,7172 8,561


1530,9 1512,8 1523,1 1536


-167,08 -173,37 -170,35 -164,05


28,781 24,871 27,18 29,822


1,3078 1,2581 1,2811 1,3332


13200 13369 13277 13150


1799,5 1799,5 1799,5 1799,5


650,59 485,83 580,21 698,49



ATMOSPHERIC DISPERSION Case description: B13_liquifier to tank - dispersion D3 (linked to Pool evaporation - B13_liquifier to tank - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release))



Model: Dense Gas Dispersion: Explosive mass version: 5.13 (07/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B13_liquifier to tank - dispersion D9 (linked to Pool evaporation - B13_liquifier to tank - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) compared to: B13_liquifier to tank - dispersion E5 (linked to Pool evaporation - B13_liquifier to tank - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) compared to: B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) Parameters

Inputs

B13_liquifier to tank -dispersion D3 (linked to

Pool evaporation -B13_liquifier to tank -



B13_liquifier to tank -release))






B13_liquifier to tank -dispersion E5 (linked to





B13_liquifier to tank -dispersion F2 (linked to











releaseTotal mass released (kg)

13479 13479 13479 13479


8,6222 8,8372 8,7172 8,561


1530,9 1512,8 1523,1 1536



650,59 485,83 580,21 698,49



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0

Ambient relative 75 75 75 75



humidity (%) Roughness length description



1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results











B13_liquifier to tank -dispersion E5 (linked to





B13_liquifier to tank -dispersion F2 (linked to






0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 460,15

...at time tmem (s)

0 0 0 1500


0 0 0 105,22


0 0 0 1536


0 0 0 127,82


0 0 0 42,894


0 0 0 -15,957


0 0 0 4607

...at time tmac (s) 0 0 0 1536




0 0 0 460,15


0 0 0 127,82


0 0 0 42,894


0 0 0 -15,957


0 0 0 47,953


0 0 0,011686 0,04733



16:42:11

EXPLOSION Case description: B13_liquifier to tank - uvce F2 LC1 (linked to Dense Gas Dispersion: Explosive mass - B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release))) Model: Explosion (Multi Energy model) version: 5.03 (25/06/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions Parameters Inputs Chemical name (DIPPR) METHANE (DIPPR)Ambient pressure (bar) 1,0151Total mass in explosive range (kg) 460,15Fraction of flammable cloud confined (%) 8Curve number 3 (Weak deflagration)Distance from release (Xd) (m) 50Offset between release point and cloud centre (m)

47,953

Threshold overpressure (mbar) 168X-coordinate of release (m) 0Y-coordinate of release (m) 0Predefined wind direction NWind comes from (North = 0 degrees) (deg)

0

Results Confined mass in explosive range (kg) 36,812Total combustion energy (MJ) 1841,7Peak overpressure at Xd (mbar) 17,35Peak dynamic pressure at Xd (mbar) 1,0151Pressure impulse at Xd (Pa*s) 135,96Positive phase duration at Xd (ms) 156,73




-1E100

Blast-wave shape at Xd Pressure waveDamage (general description) at Xd No damage or very minor damage

Damage to brick houses at Xd Damage to roofs, ceilings, minor crack formation in plastering, more

than 1% damage to glass panels (1 - 1.5 kPa)Damage to typical American-style houses at Xd


Damage to structures (empirical) at Xd No damage or very minor damage Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010


POOL FIRE Case description: B13_liquifier to tank - PFIRE D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) Model: Pool fire version: 5.11 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B13_liquifier to tank - PFIRE D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - PFIRE E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - PFIRE F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) Parameters

Inputs

B13_liquifier to tank -PFIRE D3 (linked to


model) - B13_liquifier to tank - release)

B13_liquifier to tank - PFIRE D9 (linked to



B13_liquifier to tank -PFIRE E5 (linked to



B13_liquifier to tank -PFIRE F2 (linked to








13479 13479 13479 13479


9,1505 9,1505 9,1505 9,1505


1473 1473 1473 1473


2206 2206 2206 2206


0 0 0 0


0 0 0 0

Hole diameter (mm)

101,6 101,6 101,6 101,6


1 1 1 1

Initial height of



the liquid above release point (m) Cross-sectional area of the tank (m2)

Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




6,8 6,8 6,8 6,8


9,23 9,23 9,23 9,23


13,4 13,4 13,4 13,4




Results

B13_liquifier to tank -PFIRE D3 (linked to



B13_liquifier to tank - PFIRE D9 (linked to



B13_liquifier to tank -PFIRE E5 (linked to



B13_liquifier to tank -PFIRE F2 (linked to




52,998 52,998 52,998 52,998


0,024267 0,016833 0,020802 0,026237


102,57 99,201 102,58 99,747


91,122 90,931 92,641 87,758


77,746 81,665 81,169 73,724


172,07 172,07 172,07 172,07


78,335 78,335 78,335 78,335


67,437 77,051 71,399 67,437


45,663 46,794 46,143 45,663


772,73 807,96 787,68 772,73


57,115 46,034 52,082 57,115


2206 2206 2206 2206


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69








RISK ZONES CALCULATIONS B.01A FLASHF Case description: B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)) compared to: B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)) compared to: B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)) Parameters

Inputs

B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge(TPDIS model) -B01a_TANK_G1_RELEASE))

B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE))

B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE))

B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE))



Type of release



3,0878E07 3,0878E07 3,0878E07 3,0878E07


118,62 116,07 99,648 133,75


757,41 1565,7 1219,4 561,47



2206 2206 2206 2206



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0

Z-



coordinate (height) of release (m) Ambient temperature (°C)

19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75


High crops; scattered large objects, 15 < x/h < 20.





1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results



B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE))

B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE))


0 0 0 0

Height to LEL at time

0 0 0 0



t (m) Length of cloud (between LEL) at time t (m)

0 0 0 0


0 0 0 0


0 0 0 0


5155 0 2985,6 3,2752E05

...at time tmem (s)

100 2000 1200 700


90,355 0 95 693,35


757,41 2000 1219,4 731,73


275,68 0 269,9 1841


73,367 0 71,114 1974,9


-30,456 0 -29,729 71,699


15595 0 14130 6,7748E05

...at time tmac (s)

757,41 1565,7 1219,4 700

Explosive 5155 0 2985,6 3,2752E05



mass at time tmac (kg) Length of cloud (between LEL) at time tmac (m)

275,9 0 269,9 1841


73,352 0 71,114 1974,9


-30,456 0 -29,729 71,699


107,49 0 105,22 992,22


0 0 0,012352 0,048833

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:01:22 UVCE Case description: B01a_TANK_G1_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01a_TANK_G1_D3_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_D9_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_D9_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_D9_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -



B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Parameters

Inputs

B01a_TANK_G1_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))


B01a_TANK_G1_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))




B01a_TANK_G1_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

Chemical name (DI

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)



PPR) Ambient pressure (bar)

1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


5155 5155 5155 0 0 0 2985,6 2985,6 2985,6 3,2752E05

3,2752E05

3,2752E05


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














50 50 50 50 50 50 50 50 50 50 50 50

Offset between release point an

107,49 107,49 107,49 0 0 0 105,22 105,22 105,22 992,22 992,22 992,22



d cloud centre (m) Threshold overpressure (mbar)

170 360 900 170 360 900 170 360 900 160 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Result

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1

B01a_TANK_G1



s _D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

_D3_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))




_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))


412,4 412,4 412,4 0 0 0 238,85 238,85 238,85 26201 26201 26201


20633 20633 20633 -1E94 -1E94 -1E94 11950 11950 11950 1,3109E06

1,3109E06

1,3109E06

Peak overpress

143,9 143,9 143,9 -1E98 -1E98 -1E98 119,14 119,14 119,14 206,07 206,07 206,07



ure at Xd (mbar) Peak dynamic pressure at Xd (mbar)

20,924 20,924 20,924 -1E98 -1E98 -1E98 13,575 13,575 13,575 68,044 68,044 68,044


843,2 843,2 843,2 -1E100 -1E100 -1E100 587,9 587,9 587,9 5106,8 5106,8 5106,8


117,2 117,2 117,2 -1E103 -1E103 -1E103 98,69 98,69 98,69 495,65 495,65 495,65


42,13 -1E100 -1E100 -1E100 -1E100 -1E100 35,117 -1E100 -1E100 178,78 -1E100 -1E100

Blast-

Pressure wave

Pressure wave

Pressure wave

*** NOT INITIALI

*** NOT INITIALI

*** NOT INITIALI

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave



wave shape at Xd

ZED ZED ZED















Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed, serious damage to the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).













Minor damage. Comparable to a damage due to a storm; wooden walls fail, breakage of windows (7-10 kPa).









Moderate to minor damage. Deformed walls and doors; failure of joints. Doors and window frames have failed.





Wall covering has fallen down (15 kPa).




Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).









Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connect





ions between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).



Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 9:49:39 UVCE ED Case description: B01a_TANK_G1_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01a_TANK_G1_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Parameters

Inputs

B01a_TANK_G1_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))




1,0151 1,0151 1,0151 1,0151

Total mass in

5155 0 2985,6 3,2752E05



explosive range (kg) Fraction of flammable cloud confined (%)

8 8 8 8

Curve number



50 50 50 50


107,49 0 105,22 992,22


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

B01a_TANK_G1_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01a_TANK_G1_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))

B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01a_TANK_G1_RELEASE)))


412,4 0 238,85 26201


20633 -1E94 11950 1,3109E06

Peak 143,9 -1E98 119,14 206,07



overpressure at Xd (mbar) Peak dynamic pressure at Xd (mbar)

20,924 -1E98 13,575 68,044


843,2 -1E100 587,9 5106,8


117,2 -1E103 98,69 495,65


44,805 -1E100 37,347 178,78






Minor damage (Zone D:3.5 - 17 kPa).











Moderate to minor damage. Deformed walls and doors; failure of joints. Doors and window frames have failed. Wall covering has fallen down (15 kPa).





Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed



(15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:13:23 PFIRE Case description: B01a_TANK_G1_PFIRE D3 RZ Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B01a_TANK_G1_PFIRE D9 RZ compared to: B01a_TANK_G1_PFIRE E5 RZ compared to: B01a_TANK_G1_PFIRE F2 RZ Parameters

Inputs B01a_TANK_G1_PFIRE D3 RZ

B01a_TANK_G1_PFIRE D9 RZ

B01a_TANK_G1_PFIRE E5 RZ

B01a_TANK_G1_PFIRE F2 RZ






3,0878E07 3,0878E07 3,0878E07 3,0878E07




2206 2206 2206 2206


0 0 0 0


0 0 0 0

Hole diameter (mm)




Pool thickness



(mm) Temperature of the pool (°C)

19 19 19 19

Pool burning rate




35 35 35 35

Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/Default Value of soot fraction (-)


3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


20 20 20 20


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3




13,4 13,4 13,4 13,4


Results B01a_TANK_G1_PFIRE D3 RZ

B01a_TANK_G1_PFIRE D9 RZ

B01a_TANK_G1_PFIRE E5 RZ

B01a_TANK_G1_PFIRE F2 RZ


52,998 52,998 52,998 52,998


0,024267 0,016833 0,020802 0,026237


99,788 97,293 100,15 96,947


90,835 90,721 92,406 87,471


77,746 81,665 81,169 73,724


172,07 172,07 172,07 172,07


1,7945E05 1,7945E05 1,7945E05 1,7945E05


67,437 77,051 71,399 67,437

Flame tilt (deg)

40,884 56,324 48,526 34,492

View factor (%)

0,078803 0,046687 0,063139 0,085203


45,663 46,794 46,143 45,663


772,73 807,96 787,68 772,73


57,115 46,034 52,082 57,115


2206 2206 2206 2206


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4




224,69 224,69 224,69 224,69

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 8:30:59



B.01b FLASHF Case description: B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (06/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)) compared to: B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)) compared to: B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)) Parameters

Inputs

B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation -B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE))


B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE))

B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE))



Type of release



3,0818E07 3,0818E07 3,0818E07 3,0818E07


88,095 103,06 81,915 94,007


977,36 1674,9 1424,1 761,46



743,84 894,91 656,72 827,07



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0

Z-coordinate (height) of



release (m) Ambient temperature (°C)

19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75







1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results



B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE))

B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE))


0 72,098 0 0


0 4 0 0

Length of 0 18,719 0 0



cloud (between LEL) at time t (m) Width of cloud (between LEL) at time t (m)

0 40,156 0 0


0 -18,587 0 0


5250,3 698,1 2295,8 8,3549E05

...at time tmem (s)

800 500 1400 800


97,97 95 95 794,96


977,36 1674,9 1424,1 805


322,09 122,76 113,38 2306,5


49,314 42,957 46,598 1582,6


-18,379 -18,587 -17,229 -23,107


11264 3958,2 4759,4 1,3723E06

...at time tmac (s)

977,36 1674,9 1424,1 800

Explosive mass at time tmac

5250,3 698,1 2295,8 8,3549E05



(kg) Length of cloud (between LEL) at time tmac (m)

322,09 18,719 113,38 2306,5


49,314 40,156 46,598 1582,6


-18,379 -18,587 -17,229 -23,107


142,67 -9,2275 39,459 1130,1


0 0 0,012352 0,048833

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:14:37 UVCE Case description: B01b_TANK_G2_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01b_TANK_G2_D3_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D9_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D9_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D9_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))



compared to: B01b_TANK_G2_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) Parameters

Inputs

B01b_TANK_G2_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation -B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


B01b_TANK_G2_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))




B01b_TANK_G2_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)




1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


5250,3 5250,3 5250,3 698,1 698,1 698,1 2295,8 2295,8 2295,8 8,3549E05

8,3549E05

8,3549E05


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














50 50 50 50 50 50 50 50 50 50 50 50

Offset between release point and clo

142,67 142,67 142,67 -9,2275 -9,2275 -9,2275 39,459 39,459 39,459 1130,1 1130,1 1130,1



ud centre (m) Threshold overpressure (mbar)

170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

B01b_TANK_G2_D3_UVCE Z1






B01b_TANK_G2_E5_UVCE Z1



B01b_TANK_G2_F2_UVCE Z1





(linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation -B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


(linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))




(linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))

(linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

(linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

(linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)))

(linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

(linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


420,02 420,02 420,02 55,848 55,848 55,848 183,66 183,66 183,66 66839 66839 66839


21014 21014 21014 2794,1 2794,1 2794,1 9188,8 9188,8 9188,8 3,344E06

3,344E06

3,344E06

Peak overpressure at

144,77 144,77 144,77 74,014 74,014 74,014 109,28 109,28 109,28 206,07 206,07 206,07



Xd (mbar) Peak dynamic pressure at Xd (mbar)

21,174 21,174 21,174 4,3341 4,3341 4,3341 11,055 11,055 11,055 68,044 68,044 68,044


853,35 853,35 853,35 229,21 229,21 229,21 495,99 495,99 495,99 6977,8 6977,8 6977,8


117,89 117,89 117,89 61,936 61,936 61,936 90,777 90,777 90,777 677,24 677,24 677,24


42,388 -1E100 -1E100 21,635 -1E100 -1E100 32,173 -1E100 -1E100 229,7 -1E100 -1E100

Blast-wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave



shape at Xd Damage (general description) at Xd

















Habitable after relatively easy repairs. Minor structural damage (3 kPa).



















Moderate to minor damage. Deformed walls and doors; failure of joints. Doors and window frames have failed. Wall coverin





g has fallen down (15 kPa).







Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).






Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between





steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).



Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 9:54:44 UVCE ED Case description: B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01b_TANK_G2_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) Parameters

Inputs

B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01b_TANK_G2_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation -B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation -B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)




1,0151 1,0151 1,0151 1,0151 1,0151


3,2752E05 5250,3 698,1 2295,8 8,3549E05


8 8 8 8 8

Curve number







50 50 50 50 50


992,22 142,67 -9,2275 39,459 1130,1


160 160 160 160 160


0 0 0 0 0


0 0 0 0 0


N N N N N


0 0 0 0 0

Results

B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation -

B01b_TANK_G2_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation -

B01b_TANK_G2_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation -

B01b_TANK_G2_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation -

B01b_TANK_G2_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation -



B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE)))

B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))

B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)))


26201 420,02 55,848 183,66 66839


1,3109E06 21014 2794,1 9188,8 3,344E06


206,07 144,77 74,014 109,28 206,07


68,044 21,174 4,3341 11,055 68,044


5106,8 853,35 229,21 495,99 6977,8


495,65 117,89 61,936 90,777 677,24


178,78 45,079 23,008 34,216 244,28


Pressure wave Pressure wave Pressure wave Pressure wave Pressure wave








Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed, serious







damage to the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).





Minor damage. Comparable to a damage due to a storm; wooden walls fail, breakageof windows (7-10 kPa).





Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).





Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:13:57 PFIRE Case description: B01b_TANK_G2_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B01b_TANK_G2_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) compared to: B01b_TANK_G2_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) compared to: B01b_TANK_G2_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE) Parameters



Inputs

B01b_TANK_G2_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)






3,0818E07 3,0818E07 3,0818E07 3,0818E07


8363,6 8363,6 8363,6 8363,6


1800 1800 1800 1800


10000 10000 10000 10000


0 0 0 0


0 0 0 0

Hole diameter (mm)

1000 1000 1000 1000


1 1 1 1



Pool thickness (mm)


19 19 19 19

Pool Calculate/Default Calculate/Default Calculate/Default Calculate/Default



burning rate Value of pool burning rate (kg/m2*s)


35 35 35 35

Soot Fraction




3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


20 20 20 20


No No No No


0 0 0 0


0 0 0 0


N N N N

Wind comes from (North = 0 degrees)

0 0 0 0



(deg) Calculate all contours for



7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results

B01b_TANK_G2_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)

B01b_TANK_G2_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01_b_TANK_G2_RELEASE)


112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194


193,84 189,89 195,74 189,66


177,13 176,96 180,56 172,11


153,44 159,19 159,19 147,33


780 780 780 780

Duration of the pool fire

39511 39511 39511 39511



(s) Heat emission from fire surface (kW/m2)

78,846 87,066 80,77 78,846

Flame tilt (deg)

37,614 53,697 45,489 31,201

View factor (%)

0,30773 0,19824 0,26527 0,32729


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.01c FLASHF Case description: B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (21/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)) compared to: B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)) compared to: B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)) Parameters

Inputs

B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE))


B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE))

B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE))



Type of release



3,078E07 3,078E07 3,078E07 3,078E07


74,107 74,107 74,107 74,107


1086,9 1086,9 1086,9 1086,9



1020,4 1020,4 1020,4 1020,4



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0





19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75







1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results



B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE))

B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE))


0 0 0 0


0 0 0 0

Length of 0 0 0 0



cloud (between LEL) at time t (m) Width of cloud (between LEL) at time t (m)

0 0 0 0


0 0 0 0


3034,8 241,91 2737 9598,2

...at time tmem (s)

1000 500 800 900

Start timewhere 95% of maximum of explosive mass is reached (s)

95 95 95 497,41


1086,9 1086,9 1086,9 1086,9


234,05 79,974 305,88 1089,3


52,418 37,178 52,774 139,78


-21,027 -18,377 -20,89 -21,886


9142,9 2360,6 10202 18873

...at time tmac (s)

1086,9 1086,9 1086,9 1086,9

Explosive mass at time tmac

3034,8 241,91 2737 9598,2



(kg) Length of cloud (between LEL) at time tmac (m)

234,05 18,372 305,88 1089,3


52,418 34,313 52,774 139,78


-21,027 -18,377 -20,89 -21,886


95,996 -9,1906 132,05 522,75


0 0 0,012352 0,048833

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:16:20 UVCE Case description: B01c_TANK_G3_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01c_TANK_G3_D3_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_D9_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_D9_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_D9_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -



B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Parameters

Inputs

B01c_TANK_G3_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))


B01c_TANK_G3_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))




B01c_TANK_G3_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))

B01c_TANK_G3_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

B01c_TANK_G3_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

B01c_TANK_G3_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))

B01c_TANK_G3_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

B01c_TANK_G3_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))


METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)




1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


3034,8 3034,8 3034,8 241,91 241,91 241,91 2737 2737 2737 9598,2 9598,2 9598,2


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














50 50 50 50 50 50 50 50 50 50 50 50


95,996 95,996 95,996 -9,1906 -9,1906 -9,1906 132,05 132,05 132,05 522,75 522,75 522,75




170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

B01c_TANK_G3_D3_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3


B01c_TANK_G3_D3_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3




B01c_TANK_G3_E5_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3

B01c_TANK_G3_E5_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3

B01c_TANK_G3_E5_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3

B01c_TANK_G3_F2_UVCE Z1 (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3

B01c_TANK_G3_F2_UVCE Z2 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3

B01c_TANK_G3_F2_UVCE Z3 (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3



_DISPERSION D3 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))


_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))




_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))

_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)))

_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))

_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)))


242,78 242,78 242,78 19,353 19,353 19,353 218,96 218,96 218,96 767,86 767,86 767,86


12147 12147 12147 968,22 968,22 968,22 10955 10955 10955 38417 38417 38417


119,8 119,8 119,8 52,775 52,775 52,775 115,68 115,68 115,68 176,28 176,28 176,28

Peak dynamic

13,744 13,744 13,744 1,7912 1,7912 1,7912 12,711 12,711 12,711 33,368 33,368 33,368



pressure at Xd (mbar) Pressure impulse at Xd (Pa*s)

594,2 594,2 594,2 116,46 116,46 116,46 555,48 555,48 555,48 1265,2 1265,2 1265,2


99,197 99,197 99,197 44,136 44,136 44,136 96,035 96,035 96,035 143,54 143,54 143,54


35,309 -1E100 -1E100 15,196 -1E100 -1E100 34,114 -1E100 -1E100 51,829 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Damage (general des















cription) at Xd



























Damage to structur










Walls made of concrete blocks have collapse





es (empirical) at Xd







d (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).



Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 10:44:13 UVCE ED Case description: B01c_TANK_G3_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01c_TANK_G3_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Parameters

Inputs

B01c_TANK_G3_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -

B01c_TANK_G3_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -

B01c_TANK_G3_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -

B01c_TANK_G3_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -



B01c_TANK_G3_RELEASE)))







1,0151 1,0151 1,0151 1,0151


2669,8 188,03 2389,4 5113,2


8 8 8 8

Curve number



50 50 50 50


87,82 -9,0757 117,68 20,831


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

B01c_TANK_G3_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEA

B01c_TANK_G3_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEA

B01c_TANK_G3_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEA

B01c_TANK_G3_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass -B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEA



SE))) SE))) SE))) SE))) Confined mass in explosive range (kg)

213,58 15,042 191,15 409,06


10686 752,59 9563,4 20466


114,71 48,506 110,69 143,49


12,474 1,4844 11,416 20,814


546,5 99,315 508,89 838,58


95,281 40,949 91,948 116,89


35,981 14,859 34,674 44,683

























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:14:31 PFIRE Case description: B01b_TANK_G3_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B01b_TANK_G3_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE) compared to: B01b_TANK_G3_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE) compared to: B01b_TANK_G3_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE) Parameters

Inputs

B01b_TANK_G3_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)






3,078E07 3,078E07 3,078E07 3,078E07


767,31 767,31 767,31 767,31


1800 1800 1800 1800


10000 10000 10000 10000


0 0 0 0


0 0 0 0

Hole diameter (mm)

300 300 300 300




1 1 1 1



Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35

Soot Fraction




3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


20 20 20 20


No No No No


0 0 0 0




0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results

B01b_TANK_G3_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)

B01b_TANK_G3_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B01c_TANK_G3_RELEASE)


112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194


193,84 189,89 195,74 189,66

Heat radiation second contour at

177,13 176,96 180,56 172,11



(m) Heat radiation third contour at (m)

153,44 159,19 159,19 147,33


780 780 780 780


39462 39462 39462 39462


78,846 87,066 80,77 78,846

Flame tilt (deg)

37,614 53,697 45,489 31,201

View factor (%)

0,30773 0,19824 0,26527 0,32729


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.02A FLASHF Case description: HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (21/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9) compared to: HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5) compared to: HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2) Parameters

Inputs

HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3)


HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION E5)

HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2)



Type of release




1897,4 1897,4 1897,4 1897,4


88,987 88,987 88,987 88,987



29050 29050 29050 29050



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0





19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




120 120 120 120


20 20 20 20


Low Low Low Low

Results






83051 0 1,0599E05 1,295E05


30,9 0 48,9 14,2

Length of cloud (between

375,91 0 463,58 477,85



LEL) at time t (m) Width of cloud (between LEL) at time t (m)

258,06 0 268,83 329,6


114,38 0 82,945 -128,47


95753 35000 1,2303E05 1,303E05

...at time tmem (s)

100 80 100 100


377,45 530,53 445,59 453,6


267,16 218,5 288,05 324,59


51,042 -102,87 -3,7793 -140,57


84330 91561 1,126E05 2,7644E05

...at time tmac (s)

100 88,987 88,987 350


95753 35000 1,0534E05 53731


377,45 530,53 487,5 611,5


267,16 218,5 287,39 545,94


51,042 -102,87 -113,52 229,83



location and LEL at time tmac (m) Offset between release centre and cloud centre at time tmac (m)

239,77 162,39 130,23 535,58


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:26:22 UVCE Case description: HARDARM_L1_L_UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L1_L_UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: HARDARM_L1_L_UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: HARDARM_L1_L_UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L1_L_UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L1_L_UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L1_L_UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) compared to: HARDARM_L1_L_UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) compared to: HARDARM_L1_L_UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) Parameters

Inputs

HARDARM_L1_L_UVCE D3 Z1 (linked to Dense Gas Dispersi






HARDARM_L1_L_UVCE E5 Z1 (linked to Dense Gas Dispersi



HARDARM_L1_L_UVCE F2 Z1 (linked to Dense Gas Dispersi





on: Explosive mass -HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3))






on: Explosive mass -HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION E5))



on: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))




METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


95753 95753 95753 35000 35000 35000 1,0534E05

1,0534E05

1,0534E05

53731 53731 53731


8 8 8 8 8 8 8 8 8 8 8 8

Cu 5 5 5 5 5 5 5 5 5 5 5 5



rve number

(Medium deflagration)













100 100 100 100 100 100 100 100 100 100 100 100


239,77 239,77 239,77 162,39 162,39 162,39 130,23 130,23 130,23 535,58 535,58 535,58


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0

Y-coordinate of relea

0 0 0 0 0 0 0 0 0 0 0 0



se (m) Predefined wind direction



0 0 0 0 0 0 0 0 0 0 0 0

Results

HARDARM_L1_L_UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3))






HARDARM_L1_L_UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION E5))



HARDARM_L1_L_UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))



Confined mass in explo

7660,2 7660,2 7660,2 2800 2800 2800 8427,4 8427,4 8427,4 4298,5 4298,5 4298,5



sive range (kg) Total combustion energy (MJ)

3,8325E05

3,8325E05

3,8325E05

1,4009E05

1,4009E05

1,4009E05

4,2163E05

4,2163E05

4,2163E05

2,1506E05

2,1506E05

2,1506E05


186,89 186,89 186,89 135,85 135,85 135,85 191,52 191,52 191,52 156,71 156,71 156,71


39,918 39,918 39,918 18,348 18,348 18,348 42,915 42,915 42,915 25,521 25,521 25,521


2885,9 2885,9 2885,9 1511,4 1511,4 1511,4 3052,3 3052,3 3052,3 2001,1 2001,1 2001,1

Positive phase durati

308,84 308,84 308,84 222,52 222,52 222,52 318,75 318,75 318,75 255,38 255,38 255,38



on at Xd (ms) Dist. from center mass of cloud at threshold overpressure (m)

111,57 -1E100 -1E100 79,775 -1E100 -1E100 115,18 -1E100 -1E100 92,028 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave















Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed,














serious damage to the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).















Moderate tominor damage. Deformed walls and doors; failure of joints. Doors and window frames have failed. Wall covering has fallen down (15 kPa).











Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 9:21:45 UVCE ED Case description: HARDARM_L1_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L1_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L1_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) Parameters

Inputs

HARDARM_L1_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3))


HARDARM_L1_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION E5))

HARDARM_L1_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))




1,0151 1,0151 1,0151 1,0151


95750 35000 1,0534E05 53731


8 8 8 8

Curve number



100 100 100 100

Offset between release point and cloud

239,77 162,39 130,23 535,58



centre (m) Threshold overpressure (mbar)

160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results






7660 2800 8427,4 4298,5


3,8324E05 1,4009E05 4,2163E05 2,1506E05


186,89 135,85 191,52 156,71


39,917 18,348 42,915 25,521


2885,9 1511,4 3052,3 2001,1

Positive phase

308,84 222,52 318,75 255,38



duration at Xd (ms) Dist. from center mass of cloud at threshold overpressure (m)

118,66 84,841 122,49 97,871



















Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).




Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 12:06:29 PFIRE Case description: HARDARM_L1_L_PFIRE D3 RZ Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: HARDARM_L1_L_PFIRE D9 RZ compared to: HARDARM_L1_L_PFIRE E5 RZ compared to: HARDARM_L1_L_PFIRE F2 RZ Parameters

Inputs HARDARM_L1_L_PFIRE D3 RZ

HARDARM_L1_L_PFIRE D9 RZ

HARDARM_L1_L_PFIRE E5 RZ

HARDARM_L1_L_PFIRE F2 RZ








19298 19298 19298 19298




10000 10000 10000 10000


0 0 0 0


0 0 0 0

Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19

Ambient 75 75 75 75



relative humidity (%) Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results HARDARM_L1_L_PFIRE D3 RZ





112,84 112,84 112,84 112,84




0,11465 0,083056 0,10169 0,12194


193,84 189,89 195,74 189,66


177,13 176,96 180,56 172,11


153,44 159,19 159,19 147,33


780 780 780 780


24,741 24,741 24,741 24,741


78,846 87,066 80,77 78,846

Flame tilt (deg)

37,614 53,697 45,489 31,201

View factor (%)

0,30773 0,19824 0,26527 0,32729


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69

Other information



Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 8:47:38



B.02B FLASHF Case description: HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (19/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9) compared to: HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5) compared to: HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2) Parameters

Inputs







Type of release




89,069 89,069 89,069 89,069


126,64 126,64 126,64 126,64



1363,7 1363,7 1363,7 1363,7



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0





19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




120 120 120 120


20 20 20 20


Low Low Low Low

Results






3548,4 242,34 3208 7152


11,2 4,8 8,6 22,8


227,39 79,558 300,58 99,999



LEL) at time t (m) Width of cloud (between LEL) at time t (m)

59,721 39,748 59,49 131,1


-24,116 -19,405 -23,94 -25,165


3548,9 242,37 3208 7311,5

...at time tmem (s)

80 10 120 125


68,149 9,5 61,777 104,53


126,64 126,64 126,64 127,82


215,92 79,552 300,58 99,999


59,276 39,748 59,49 131,1


-24,116 -19,405 -23,94 -25,165


13636 2524,4 12857 28278

...at time tmac (s)

130 126,64 130 250

Explosive 3067,5 242,34 1814,7 2837,5



mass at time tmac (kg) Length of cloud (between LEL) at time tmac (m)

320,02 79,558 502,13 123,92


63,344 39,748 36,488 300,84


-8,0251 -19,405 -11,317 229,56


151,98 20,374 239,75 291,52


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:27:18 UVCE Case description: HARDARM_L2_L_UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L2_L_UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) compared to: HARDARM_L2_L_UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) compared to: HARDARM_L2_L_UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass -



HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) compared to: HARDARM_L2_L_UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) compared to: HARDARM_L2_L_UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs














METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151

Total mass in explosive range (kg

3067,5 3067,5 3067,5 242,34 242,34 242,34 1814,7 1814,7 1814,7 2837,5 2837,5 2837,5



) Fraction of flammable cloud confined (%)

8 8 8 8 8 8 8 8 8 8 8 8

Curve number














100 100 100 100 100 100 100 100 100 100 100 100


151,98 151,98 151,98 20,374 20,374 20,374 239,75 239,75 239,75 291,52 291,52 291,52


170 360 900 170 360 900 170 360 900 170 360 900




0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

HARDARM_L2_L_UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L2_L_DISPERSION D3






HARDARM_L2_L_UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L2_L_DISPERSION E5



HARDARM_L2_L_UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L2_L_DISPERSION F2





(linked to Pool evaporation -HARDARM_L2_L_EVAPORATION D3))






(linked to Pool evaporation -HARDARM_L2_L_EVAPORATION E5))



(linked to Pool evaporation -HARDARM_L2_L_EVAPORATION F2))




245,4 245,4 245,4 19,387 19,387 19,387 145,18 145,18 145,18 227 227 227


12278 12278 12278 969,98 969,98 969,98 7263,4 7263,4 7263,4 11357 11357 11357


60,772 60,772 60,772 25,904 25,904 25,904 51,851 51,851 51,851 59,221 59,221 59,221


2,631 2,631 2,631 1,0151 1,0151 1,0151 1,7118 1,7118 1,7118 2,4677 2,4677 2,4677

Pres

310,81 310,81 310,81 58,124 58,124 58,124 224,51 224,51 224,51 295,27 295,27 295,27



sure impulse at Xd (Pa*s) Positive phase duration at Xd (ms)

102,29 102,29 102,29 44,876 44,876 44,876 86,599 86,599 86,599 99,718 99,718 99,718


35,436 -1E100 -1E100 15,205 -1E100 -1E100 29,747 -1E100 -1E100 34,527 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Shock Wave

Shock Wave

Shock Wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Damage (general descr















iption) at Xd





Damage to roofs, ceilings, minor crack formation in plastering, more than 1% damage to glass panels (1 - 1.5 kPa)
































No damage or veryminor damage



Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 9:26:44 UVCE ED Case description: HARDARM_L2_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3))



Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L2_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs








1,0151 1,0151 1,0151 1,0151


3067,5 242,34 1814,7 2837,5


8 8 8 8

Curve number



100 100 100 100


151,98 20,374 239,75 291,52


160 160 160 160


0 0 0 0

Y-coordinate of release

0 0 0 0



(m) Predefined wind direction

N N N N


0 0 0 0

Results






245,4 19,387 145,18 227


12278 969,98 7263,4 11357


60,772 25,904 51,851 59,221


2,631 1,0151 1,7118 2,4677


310,81 58,124 224,51 295,27


102,29 44,876 86,599 99,718


37,686 16,17 31,636 36,719


Pressure wave Shock Wave Pressure wave Pressure wave

Damage (general







description) at Xd
















Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 12:09:37 PFIRE Case description: HARDARM_L2_L_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: HARDARM_L2_L_PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy) compared to: HARDARM_L2_L_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy) compared to: HARDARM_L2_L_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy) Parameters

Inputs

HARDARM_L2_L_PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy)


HARDARM_L2_L_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy)

HARDARM_L2_L_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy)






0,003991 0,003991 0,003991 0,003991


3,3103E-05 3,3103E-05 3,3103E-05 3,3103E-05


120 120 120 120


10000 10000 10000 10000

Height of the 0 0 0 0



observer position above ground level (m) Height of the confined pool above ground level (m)

0 0 0 0

Hole diameter (mm)

0,15 0,15 0,15 0,15


0,62 0,62 0,62 0,62

Initial height of the liquidabove release point (m)


Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75

Take protective

No No No No



effects of clothing into account X-coordinate of release (m)

0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results



HARDARM_L2_L_PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy)

HARDARM_L2_L_PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - ship-shore b rev release copy)


112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194


193,84 189,89 195,74 189,66


177,13 176,96 180,56 172,11




153,44 159,19 159,19 147,33


780 780 780 780


5,1167E-06 5,1167E-06 5,1167E-06 5,1167E-06


78,846 87,066 80,77 78,846

Flame tilt (deg)

37,614 53,697 45,489 31,201

View factor (%)

0,30773 0,19824 0,26527 0,32729


47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.03A FLASHF Case description: B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (06/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9) compared to: B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5) compared to: B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2) Parameters

Inputs B03a DISP D3 (linked to Pool evaporation -B03a EVAP D3)

B03a DISP D9 (linked to Pool evaporation -B03a EVAP D9)

B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)

B03a DISP F2 (linked to Pool evaporation -B03a EVAP F2)

Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Type of release Evaporating pool release




Total mass released (kg) Mass flow rate of the source (kg/s)

774,5 774,5 774,5 774,5


54,938 54,938 54,938 54,938


Fixed pool surface (m2) 8759,1 8759,1 8759,1 8759,1 Diameter of expanded jet (m)


-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data Pasquill Pasquill Pasquill Pasquill Pasquill stability class D (Neutral) D (Neutral) E (Stable) F (Very Stable) Wind speed at 10 m height (m/s)

3 9 5 2


Predefined wind direction User defined User defined User defined User defined Wind comes from (North = 0 degrees) (deg)

270 270 270 270


75 75 75 75







120 120 120 120


20 20 20 20


Low Low Low Low

Results B03a DISP D3 (linked to Pool evaporation -B03a EVAP D3)

B03a DISP D9 (linked to Pool evaporation -B03a EVAP D9)

B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)

B03a DISP F2 (linked to Pool evaporation -B03a EVAP F2)


7228,8 0 0 28734




21,7 0 0 27


208,55 0 0 302,55


85,284 0 0 91,93


234,22 0 0 13,807


24411 8987,6 29489 32372

...at time tmem (s) 50 30 60 75 Start time where 95% of maximum of explosive mass is reached (s)

-1E100 24,509 50,255 -1E100


54,938 54,938 61,44 54,938


235,09 293,33 183,64 242,62


150,49 121,52 162,02 108,9


-17,351 -55,127 -11,818 -40,724


29801 28143 31642 52817

...at time tmac (s) 50 54,938 54,938 300 Explosive mass at time tmac (kg)

24411 8985,2 27975 8896,7


235,09 296,96 218,62 392,69


150,49 121,03 160,9 169,42


-17,351 -55,127 -61,747 318,66


100,19 93,352 47,564 515,01


0 0 0,0081 0,0385

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10: UVCE Case description: B03a UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03a UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) compared to: B03a UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) compared to: B03a UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9)) compared to: B03a UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9))



compared to: B03a UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9)) compared to: B03a UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) compared to: B03a UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) compared to: B03a UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) Parameters

Inputs

B03a UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -B03a DISP D3 (linked to Pool evaporation -B03a EVAP D3))


B03a UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3))




B03a UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5))

B03a UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass -B03a DISP E5 (linked to Pool evaporation -B03a EVAP E5))


B03a UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -B03a DISP F2 (linked to Pool evaporation -B03a EVAP F2))

B03a UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2))



METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


24411 24411 24411 8985,2 8985,2 8985,2 27975 27975 27975 8896,7 8896,7 8896,7


8 8 8 8 8 8 8 8 8 8 8 8

Curve number













Distance from release

50 50 50 50 50 50 50 50 50 50 50 50



(Xd) (m) Offset between release point and cloud centre (m)

100,19 100,19 100,19 93,352 93,352 93,352 47,564 47,564 47,564 515,01 515,01 515,01


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0


User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined


270 270 270 270 270 270 270 270 270 270 270 270

Results



B03a UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3))





B03a UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass -B03a DISP E5 (linked to Pool evaporation -B03a EVAP E5))



B03a UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2))


Confined mass in explosi

1952,9 1952,9 1952,9 718,82 718,82 718,82 2238 2238 2238 711,74 711,74 711,74



ve range (kg) Total combustion energy (MJ)

97704 97704 97704 35963 35963 35963 1,1197E05

1,1197E05

1,1197E05

35609 35609 35609


206,07 206,07 206,07 172,41 172,41 172,41 206,07 206,07 206,07 171,84 171,84 171,84


66,176 66,176 66,176 31,564 31,564 31,564 72,107 72,107 72,107 31,353 31,353 31,353


2138,5 2138,5 2138,5 1210,6 1210,6 1210,6 2277,9 2277,9 2277,9 1202,7 1202,7 1202,7


207,55 207,55 207,55 140,44 140,44 140,44 221,08 221,08 221,08 139,98 139,98 139,98


70,747 -1E100 -1E100 50,702 -1E100 -1E100 74,035 -1E100 -1E100 50,534 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave















Not habitable without major repair works. Partial roof failures, 25% of all brick walls














have failed, serious damage to the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).


























Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage



Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium











tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).



ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).









Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:44:16 UVCE ED Case description: B03a UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions



compared to: B03a UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9)) compared to: B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) Parameters

Inputs

B03a UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3))


B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5))

B03a UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2))




1,0151 1,0151 1,0151 1,0151


24411 8985,2 27975 8896,7


8 8 8 8

Curve number 5 (Medium deflagration) 5 (Medium deflagration)

5 (Medium deflagration) 5 (Medium deflagration)


50 50 50 50


100,19 93,352 47,564 515,01


160 160 160 160


0 0 0 0


0 0 0 0




270 270 270 270

Results



B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5))

B03a UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2))


1952,9 718,82 2238 711,74


97704 35963 1,1197E05 35609




206,07 172,41 206,07 171,84


66,176 31,564 72,107 31,353


2138,5 1210,6 2277,9 1202,7


207,55 140,44 221,08 139,98


75,238 53,921 78,736 53,743

























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:43:01 PFIRE Case description: B03a PFIRE D3 RZ Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B03a PFIRE D9 RZ compared to: B03a PFIRE E5 RZ compared to: B03b PFIRE F2 RZ Parameters

Inputs B03a PFIRE D3 RZ

B03a PFIRE D9 RZ

B03a PFIRE E5 RZ

B03b PFIRE F2 RZ

Chemical name (DIPPR) METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

Pool size determination Confined Confined Confined Confined Total mass released (kg) 42630 42630 42630 261,6 Mass flow rate of the source (kg/s) Duration of the release (s) Pool surface poolfire (m2) 10000 10000 10000 62 Height of the observer position above ground level (m)

0 0 0 0


0 0 0 0


Cross-sectional area of the tank (m2) Pool thickness (mm) Temperature of the pool (°C) -161,15 -161,15 -161,15 -161,15 Pool burning rate Calculate/Default Calculate/Default Calculate/Default Calculate/Default Value of pool burning rate (kg/m2*s) Fraction combustion heat radiated (%) 35 35 35 35 Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/Default Value of soot fraction (-) Wind speed at 10 m height (m/s) 3 9 5 2 Ambient temperature (°C) 19 19 19 19 Ambient relative humidity (%) 75 75 75 75 Amount of CO2 in atmosphere (%) 0,03 0,03 0,03 0,03 Distance from the centre of the pool (m)

1000 1000 1000 1000

Exposure duration to heat radiation (s) 20 20 20 20 Take protective effects of clothing into account

No No No No

X-coordinate of release (m) 0 0 0 0 Y-coordinate of release (m) 0 0 0 0 Predefined wind direction User defined User defined User defined User defined Wind comes from (North = 0 degrees) (deg)

270 270 270 270

Calculate all contours for Physical effects Physical effects Physical effects Physical effects Heat radiation level (lowest) for first contour plot (kW/m2)

7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4

Percentage of mortality for contour



calculations (%)

Results

B03a PFIRE D3 RZ

B03a PFIRE D9 RZ

B03a PFIRE E5 RZ

B03b PFIRE F2 RZ

Max Diameter of the Pool Fire (m) 112,84 112,84 112,84 8,8849 Heat radiation at X (kW/m2) 0,11465 0,083056 0,10169 0,00074604 Heat radiation first contour at (m) 193,84 189,89 195,74 20,027 Heat radiation second contour at (m) 177,13 176,96 180,56 17,79 Heat radiation third contour at (m) 153,44 159,19 159,19 13,998 Combustion rate (kg/s) 780 780 780 4,836 Duration of the pool fire (s) 54,654 54,654 54,654 54,094 Heat emission from fire surface (kW/m2)

78,846 87,066 80,77 47,584

Flame tilt (deg) 37,614 53,697 45,489 42,233 View factor (%) 0,30773 0,19824 0,26527 0,0036322 Atmospheric transmissivity (%) 47,253 48,121 47,462 43,165 Flame temperature (°C) 814,17 841,32 820,71 686,03 Height of the Flame (m) 94,407 80,225 90,764 16,99 Calculated pool surface area (m2) 10000 10000 10000 62 Weight ratio of HCL/chemical (%) 0 0 0 0 Weight ratio of NO2/chemical (%) 0 0 0 0 Weight ratio of SO2/chemical (%) 0 0 0 0 Weight ratio of CO2/chemical (%) 274,4 274,4 274,4 274,4 Weight ratio of H2O/chemical (%) 224,69 224,69 224,69 224,69 Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 8:52:37



B.03B FLASHF Case description: B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (06/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9) compared to: B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5) compared to: B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2) Parameters

Inputs B03b DISP D3 (linked to Pool evaporation -B03b EVAP D3)

B03b DISP D9 (linked to Pool evaporation -B03b EVAP D9)

B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5)

B03b DISP F2 (linked to Pool evaporation -B03b EVAP F2)



Evaporating poolrelease



Total mass released (kg) Mass flow rate of the source (kg/s)

36,671 36,671 36,671 36,671


7,2048 7,2048 7,2048 7,2048


Fixed pool surface (m2) 62 62 62 62 Diameter of expanded jet (m)


-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



14,4 14,4 14,4 14,4

Meteorological data Pasquill Pasquill Pasquill Pasquill Pasquill stability class D (Neutral) D (Neutral) E (Stable) F (Very Stable) Wind speed at 10 m height (m/s)

3 9 5 2


Predefined wind direction User defined User defined User defined User defined Wind comes from (North = 0 degrees) (deg)

270 270 270 270


77 77 77 77







120 120 120 120


20 20 20 20


Low Low Low Low

Results B03b DISP D3 (linked to Pool evaporation -B03b EVAP D3)

B03b DISP D9 (linked to Pool evaporation -B03b EVAP D9)

B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5)

B03b DISP F2 (linked to Pool evaporation -B03b EVAP F2)


0 0 0 -1E100




0 0 0 -1E100


0 0 0 -1E100


0 0 0 -1E100


0 0 0 -1E100


196,31 180,62 194,24 -1E100

...at time tmem (s) 7,5 7 7,5 -1E100 Start time where 95% of maximum of explosive mass is reached (s)

-1E100 6,4346 -1E100 -1E100


7,2048 8,2784 7,2048 -1E100


27,474 34,656 33,691 -1E100


14,767 14,82 14,773 -1E100


-6,6877 -5,2709 -5,6714 -1E100


401,46 495,91 478,28 -1E100

...at time tmac (s) 15 8 12,5 -1E100 Explosive mass at time tmac (kg)

152,77 179,75 151,83 0


36,114 38,845 43,125 -1E100


13,786 15,198 13,769 -1E100


1,9316 -1,695 2,7495 -1E100


19,989 17,728 24,312 -1,5E100


0 0 0,0081 0

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:29:17 UVCE Case description: B03b UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03b UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3)) compared to: B03b UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3)) compared to: B03b UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to



Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) compared to: B03b UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) compared to: B03b UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) Parameters

Inputs

B03b UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3))



B03b UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass -B03b DISP D9 (linked to Pool evaporation - B03bEVAP D9))



B03b UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2))




METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


152,77 152,77 152,77 179,75 179,75 179,75 0 0 0


8 8 8 8 8 8 8 8 8

Curve number











50 50 50 50 50 50 50 50 50


19,989 19,989 19,989 17,728 17,728 17,728 0 0 0


170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0




User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined

User defined


270 270 270 270 270 270 270 270 270

Results











12,222 12,222 12,222 14,38 14,38 14,38 0 0 0


611,48 611,48 611,48 719,46 719,46 719,46 -1E94 -1E94 -1E94


44,536 44,536 44,536 47,613 47,613 47,613 -1E98 -1E98 -1E98


1,2367 1,2367 1,2367 1,4296 1,4296 1,4296 -1E98 -1E98 -1E98


85,25 85,25 85,25 96,169 96,169 96,169 -1E100 -1E100 -1E100


38,284 38,284 38,284 40,396 40,396 40,396 -1E103 -1E103 -1E103


13,038 -1E100 -1E100 13,764 -1E100 -1E100 -1E100 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

*** NOT INITIALIZED

*** NOT INITIALIZED

*** NOT INITIALIZED











Damage to Habitable Habitable Habitable Habitable Habitable Habitable No No No



brick houses at Xd

after relatively easy repairs. Minor structural damage (3 kPa).






damage or very minor damage























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:45:56 UVCE ED Case description: B03b UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03b UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5)) compared to: B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) Parameters

Inputs

B03b UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3))


B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5))

B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2))




1,0151 1,0151 1,0151 1,0151


152,77 179,75 151,83 0


8 8 8 8

Curve number 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration) Distance from release (Xd) (m)

50 50 50 50


19,989 17,728 24,312 -1,5E100

Threshold 160 160 160 160



overpressure (mbar) X-coordinate of release (m)

0 0 0 0


0 0 0 0




270 270 270 270

Results



B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5))

B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2))


12,222 14,38 12,147 0


611,48 719,46 607,7 -1E94


44,536 47,613 44,432 -1E98


1,2367 1,4296 1,2296 -1E98


85,25 96,169 84,877 -1E100


38,284 40,396 38,206 -1E103


13,865 14,638 13,837 -1E100























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:43:37 PFIRE



Case description: B03b PFIRE D3 RZ Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B03b PFIRE D9 RZ compared to: B03b PFIRE E5 RZ compared to: B03b PFIRE F2 RZ Parameters

Inputs B03b PFIRE D3 RZ

B03b PFIRE D9 RZ

B03b PFIRE E5RZ

B03b PFIRE F2 RZ

Chemical name (DIPPR) METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

Pool size determination Confined Confined Confined Confined Total mass released (kg) 261,6 261,6 261,6 261,6 Mass flow rate of the source (kg/s) Duration of the release (s) Pool surface poolfire (m2) 62 62 62 62 Height of the observer position above ground level (m)

0 0 0 0


0 0 0 0


Cross-sectional area of the tank (m2) Pool thickness (mm) Temperature of the pool (°C) -161,15 -161,15 -161,15 -161,15 Pool burning rate Calculate/Default Calculate/Default Calculate/Default Calculate/Default Value of pool burning rate (kg/m2*s) Fraction combustion heat radiated (%) 35 35 35 35 Soot Fraction Calculate/Default Calculate/Default Calculate/Default Calculate/Default Value of soot fraction (-) Wind speed at 10 m height (m/s) 3 9 5 2 Ambient temperature (°C) 19 19 19 19 Ambient relative humidity (%) 75 75 75 75 Amount of CO2 in atmosphere (%) 0,03 0,03 0,03 0,03 Distance from the centre of the pool (m)

1000 1000 1000 1000

Exposure duration to heat radiation (s) 20 20 20 20 Take protective effects of clothing into account

No No No No


270 270 270 270

Calculate all contours for Physical effects Physical effects Physical effects Physical effects Heat radiation level (lowest) for first contour plot (kW/m2)

7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results B03b PFIRE D3 RZ

B03b PFIRE D9 RZ

B03b PFIRE E5 RZ

B03b PFIRE F2 RZ

Max Diameter of the Pool Fire (m) 8,8849 8,8849 8,8849 8,8849 Heat radiation at X (kW/m2) 0,0006517 0,00042763 0,00053985 0,00074604 Heat radiation first contour at (m) 20,987 20,929 21,394 20,027 Heat radiation second contour at (m) 18,759 19,205 19,304 17,79



Heat radiation third contour at (m) 15,53 17,552 16,941 13,998 Combustion rate (kg/s) 4,836 4,836 4,836 4,836 Duration of the pool fire (s) 54,094 54,094 54,094 54,094 Heat emission from fire surface (kW/m2)

50,042 57,532 53,369 47,584

Flame tilt (deg) 48,267 61,915 55,145 42,233 View factor (%) 0,003 0,0016828 0,0023132 0,0036322 Atmospheric transmissivity (%) 43,41 44,17 43,728 43,165 Flame temperature (°C) 698,08 732,27 713,71 686,03 Height of the Flame (m) 15,603 12,388 14,016 16,99 Calculated pool surface area (m2) 62 62 62 62 Weight ratio of HCL/chemical (%) 0 0 0 0 Weight ratio of NO2/chemical (%) 0 0 0 0 Weight ratio of SO2/chemical (%) 0 0 0 0 Weight ratio of CO2/chemical (%) 274,4 274,4 274,4 274,4 Weight ratio of H2O/chemical (%) 224,69 224,69 224,69 224,69 Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 8:53:15



B04A JFIRE Case description: B04a_D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (06/11/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B04a_D9 compared to: B04a_E5 compared to: B04a_F2 Parameters Inputs B04a_D3 B04a_D9 B04a_E5 B04a_F2 Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)

Type of release Release from vessel through (a hole in) pipe

Release from vessel through (a hole in) pipe

Release from vessel through (a hole in)pipe


Pipeline length (m) 30 30 30 30 Pipeline diameter (inch) 12 12 12 12 Pipeline roughness (mm) 0,045 0,045 0,045 0,045 Hole diameter (inch) 12 12 12 12 Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges Discharge coefficient (-) 1 1 1 1 Initial temperature in vessel (°C)

-151 -151 -151 -151


1,03 1,03 1,03 1,03


45 45 45 45


1 1 1 1


3 9 5 2

Ambient temperature (°C) 19 19 19 19 Ambient relative humidity (%)

75 75 75 75

Flame temperature (°C) 926,85 926,85 926,85 926,85 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


270 270 270 270

Results B04a_D3 B04a_D9 B04a_E5 B04a_F2 Initial source strength (kg/s) 3,3751 3,3751 3,3751 3,3751 Type of flow of the jet Unchoked flow Unchoked flow Unchoked flow Unchoked flow Exit velocity of expanding jet (m/s)

28,824 28,824 28,824 28,824


0 16,056 1,5266 0

Frustum lift off height (b) (m) 6,21 0,37833 0,55996 6,939 Width of frustum base (W1) (m)

3,0683 1,256 2,203 3,6564


13,905 10,274 12,028 15,024


24,84 23,948 26,409 27,756




0 15,81 1,4949 0


837,08 525,5 717,94 1019,1


775,4 485,94 669,9 951,5


65,622 104,71 75,956 53,477


65,622 104,71 75,956 53,477


68,48 68,1 68,157 68,545

View factor (%) 0,86995 0,42126 0,68539 1,1076 Heat radiation at Xd (kW/m2)

0,39164 0,30183 0,3556 0,40675

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:32:17 FLASHF Case description: HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (25/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9) compared to: HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5) compared to: HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2) Parameters

Inputs







Type of release




1022,1 1022,1 1022,1 1022,1


165,32 165,32 165,32 165,32

Initial liquid mass fraction



(%) Fixed pool surface (m2)

10000 10000 10000 10000



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




120 120 120 120




20 20 20 20


Low Low Low Low

Results






89932 20467 54341 94021


41,2 14,8 46,9 10,5


332 451,86 262,22 427,26


178,32 146,06 181,66 292,22


-67,623 -63,147 -67,576 -127,38


1,1043E05 20467 94059 1,3065E05

...at time tmem (s)

175 150 175 175


143,95 44,841 172,04 -1E100


180,54 165,32 179,2 165,32


522,64 451,86 958,87 526,18



LEL) at time tmem (m) Width of cloud (between LEL) at time tmem (m)

160,43 146,06 320,41 339,57


1,121 -63,147 -40,879 -119,73


56523 49218 1,0773E05 1,4939E05

...at time tmac (s)

175 165,32 225 175


1,1043E05 20467 27525 1,3065E05


522,64 451,86 383,05 526,18


160,43 146,06 373,76 339,57


1,121 -63,147 758,01 -119,73


262,44 162,78 949,54 143,36


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database



Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:30:04 UVCE Case description: B04A - UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B04A - UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: B04A - UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: B04A - UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04A - UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04A - UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04A - UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: B04A - UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: B04A - UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: B04A - UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) compared to: B04A - UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) compared to: B04A - UVCEF2 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) Parameters

Inputs

B04A -UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3))






B04A -UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION E5))



B04A -UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))


B04A -UVCEF2 Z3 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))

Chemical name (DI

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)



PPR) Ambient pressure (bar)

1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


1,1043E05

1,1043E05

1,1043E05

20467 20467 20467 27525 27525 27525 1,3065E05

1,3065E05

1,3065E05


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














100 100 100 100 100 100 100 100 100 100 100 100


262,44 262,44 262,44 162,78 162,78 162,78 949,54 949,54 949,54 143,36 143,36 143,36



point and cloud centre (m) Threshold overpressure (mbar)

170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0



Wind comes from (North = 0

0 0 0 0 0 0 0 0 0 0 0 0



degrees) (deg)

Results









B04A -UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION E5 (linked toPool evaporation -HARDARM_L1_L_EVAPORATION E5))



B04A -UVCEF2 Z3 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION F2))


8834,6 8834,6 8834,6 1637,3 1637,3 1637,3 2202 2202 2202 10452 10452 10452


4,4201E05

4,4201E05

4,4201E05

81918 81918 81918 1,1017E05

1,1017E05

1,1017E05

5,2294E05

5,2294E05

5,2294E05

Peak overpressure

193,85 193,85 193,85 113,15 113,15 113,15 125 125 125 199,29 199,29 199,29



at Xd (mbar) Peak dynamic pressure at Xd (mbar)

44,49 44,49 44,49 12,063 12,063 12,063 15,101 15,101 15,101 50,575 50,575 50,575


3138,1 3138,1 3138,1 1063,5 1063,5 1063,5 1289,8 1289,8 1289,8 3439,8 3439,8 3439,8


323,77 323,77 323,77 187,97 187,97 187,97 206,36 206,36 206,36 345,21 345,21 345,21

Dist. from center mass of cloud at threshold overp

117,01 -1E100 -1E100 66,711 -1E100 -1E100 73,636 -1E100 -1E100 123,75 -1E100 -1E100



ressure (m) Blast-wave shape at Xd

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave













Moderate damage (Zone C:17 - 35 kPa).














Damage to typical America

Moderate to minor damage. Deformed walls and doors; failure of



Minor damage. Comparable to a damage due to a storm; wooden walls











n-style houses at Xd

joints. Doors and window frames have failed. Wall covering has fallen down (15 kPa).



fail, breakage of windows (7-10 kPa).






















Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 10:59:54 UVCE ED Case description: HARDARM_L1_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L1_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5))



compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs








1,0151 1,0151 1,0151 1,0151


1,1043E05 20467 27525 2837,5


8 8 8 8

Curve number



100 100 100 100


262,44 162,78 949,54 291,52


160 160 160 160


0 0 0 0


0 0 0 0


N N N N

Wind comes from

0 0 0 0



(North = 0 degrees) (deg)

Results






8834,6 1637,3 2202 227


4,4201E05 81918 1,1017E05 11357


193,85 113,15 125 59,221


44,49 12,063 15,101 2,4677


3138,1 1063,5 1289,8 295,27


323,77 187,97 206,36 99,718


124,44 70,946 78,311 36,719









Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed, serious damage to






the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).
























1407 1407 1407 1407


120 120 120 120



0 0 0 0

Height of the confined pool above ground



level (m) Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0

Y-coordinate 0 0 0 0



of release (m) Predefined wind direction

N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4







115,17 115,17 115,17 115,17


0,11963 0,086781 0,10622 0,12717


197,38 193,36 199,28 193,14


180,33 180,15 183,86 175,24


156,24 162,09 162,11 150,11


812,54 812,54 812,54 812,54


207,79 207,79 207,79 207,79

Heat emission

79,178 87,351 81,038 79,178



from fire surface (kW/m2) Flame tilt (deg)

37,525 53,623 45,405 31,113

View factor (%)

0,31943 0,20629 0,27595 0,33956


47,299 48,16 47,501 47,299


815,31 842,23 821,61 815,31


95,698 81,439 92,138 95,698


10417 10417 10417 10417


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B04B JFIRE Case description: B04b_D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (06/11/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B04b_D9 compared to: B04b_E5 compared to: B04b_F2 Parameters Inputs B04b_D3 B04b_D9 B04b_E5 B04b_F2 Chemical name (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)





Pipeline length (m) 30 30 30 30 Pipeline diameter (inch) 12 12 12 12 Pipeline roughness (mm) 0,045 0,045 0,045 0,045 Hole diameter (inch) 1,2 1,2 1,2 1,2 Hole rounding Sharp edges Sharp edges Sharp edges Sharp edges Discharge coefficient (-) 0,62 0,62 0,62 0,62 Initial temperature in vessel (°C)

-151 -151 -151 -151


1,03 1,03 1,03 1,03


45 45 45 45


1 1 1 1


3 9 5 2


75 75 75 75

Flame temperature (°C) 926,85 926,85 926,85 926,85 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


270 270 270 270

Results B04b_D3 B04b_D9 B04b_E5 B04b_F2 Initial source strength (kg/s) 0,031678 0,031678 0,031678 0,031678 Type of flow of the jet Unchoked flow Unchoked flow Unchoked flow Unchoked flow Exit velocity of expanding jet (m/s)

43,589 43,589 43,589 43,589


13,762 45,337 24,724 7,0413


0,28874 0,14976 0,22924 0,32522


1,8063 1,4413 1,6291 1,8973


3,9221 3,2229 3,5117 4,2524




12,913 44,522 23,891 6,4154


15,774 9,8636 12,578 18,008


14,631 9,0485 11,607 16,786


31,677 51,219 39,929 27,611


31,677 51,219 39,929 27,611


67,926 67,907 67,915 67,936


0,0021096 0,00060349 0,0016465 0,0023513

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:32:44 FLASHF Case description: HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (21/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9) compared to: HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5) compared to: HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2) Parameters

Inputs







Type of release




276,1 276,1 276,1 276,1


41,024 41,024 41,024 41,024





717,01 717,01 717,01 717,01



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




120 120 120 120

Concentra20 20 20 20



tion averaging time (s) Resolution of the time consuming graphs

Low Low Low Low

Results






0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


9394,5 6486,1 8413,1 8961,6

...at time tmem (s)

45 45 40 60


42,158 43,098 36,939 -1E100


48,219 45,364 45,219 41,024

Length of cloud (between LEL) at

88,49 323,78 114,97 171,61



time tmem (m) Width of cloud (between LEL) at time tmem (m)

109,21 46,432 81,54 126,01


-10,125 -12,639 -18,568 -57,713


7485,8 12769 7738,4 18153

...at time tmac (s)

45 45 41,024 60


9394,5 6486,1 8413,1 8961,6


88,49 323,78 114,97 171,61


109,21 46,432 81,54 126,01


-10,125 -12,639 -18,568 -57,713


34,12 149,25 38,915 28,09


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010



Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:30:54 UVCE Case description: B04B - UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B04B - UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: B04B - UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) compared to: B04B - UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04B - UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04B - UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: B04B - UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: B04B - UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: B04B - UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: B04B - UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) compared to: B04B - UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) compared to: B04B - UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs

B04B -UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation -HARDARM_L1_L_EVAPORATION D3))






B04B -UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation -HARDARM_L2_L_EVAPORATION E5))



B04B -UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation -HARDARM_L2_L_EVAPORATION F2))



Chemical name (DIPP

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)



R) Ambient pressure (bar)

1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


1,1043E05

1,1043E05

1,1043E05

20467 20467 20467 8413,1 8413,1 8413,1 8961,6 8961,6 8961,6


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














100 100 100 100 100 100 100 100 100 100 100 100

Offset between release poi

262,44 262,44 262,44 162,78 162,78 162,78 38,915 38,915 38,915 28,09 28,09 28,09



nt and cloud centre (m) Threshold overpressure (mbar)

170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0



Wind comes from (North = 0 de

0 0 0 0 0 0 0 0 0 0 0 0



grees) (deg)

Results














8834,6 8834,6 8834,6 1637,3 1637,3 1637,3 673,04 673,04 673,04 716,93 716,93 716,93


4,4201E05

4,4201E05

4,4201E05

81918 81918 81918 33673 33673 33673 35869 35869 35869

Peak overpressure at

193,85 193,85 193,85 113,15 113,15 113,15 84,528 84,528 84,528 86,319 86,319 86,319



Xd (mbar) Peak dynamic pressure at Xd (mbar)

44,49 44,49 44,49 12,063 12,063 12,063 5,9427 5,9427 5,9427 6,2285 6,2285 6,2285


3138,1 3138,1 3138,1 1063,5 1063,5 1063,5 596,73 596,73 596,73 621,96 621,96 621,96


323,77 323,77 323,77 187,97 187,97 187,97 141,19 141,19 141,19 144,11 144,11 144,11

Dist. from center mass of cloud at threshold overpres

117,01 -1E100 -1E100 66,711 -1E100 -1E100 49,602 -1E100 -1E100 50,657 -1E100 -1E100



sure (m) Blast-wave shape at Xd

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave







Minor damage (Zone D: 3.5 - 17kPa).




















Damage to typical American-

Moderate to minor damage. Deformed walls and doors; failure of joints.



Minor damage. Comparable to a damage due to a storm; wooden walls fail,











style houses at Xd

Doors and window frames have failed. Wall covering has fallen down (15 kPa).

























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:07:02 UVCE ED Case description: HARDARM_L2_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L2_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2))



Parameters

Inputs








1,0151 1,0151 1,0151 1,0151


3067,5 242,34 1814,7 2837,5


8 8 8 8

Curve number



100 100 100 100


151,98 20,374 239,75 291,52


160 160 160 160


0 0 0 0


0 0 0 0


N N N N

Wind comes from (North = 0

0 0 0 0



degrees) (deg)

Results






245,4 19,387 145,18 227


12278 969,98 7263,4 11357


60,772 25,904 51,851 59,221


2,631 1,0151 1,7118 2,4677


310,81 58,124 224,51 295,27


102,29 44,876 86,599 99,718


37,686 16,17 31,636 36,719













Damage No damage or very minor No damage or very minor No damage or very minor No damage or very minor



to typical American-style houses at Xd

damage damage damage damage

















94 94 94 94


120 120 120 120



0 0 0 0


Hole diameter (mm)


Initial height of the liquid above release point



(m) Cross-sectional area of the tank (m2)

Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



9 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0






7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4







36,073 36,073 36,073 36,073


0,0075699 0,0075699 0,0093922 0,012103


69,401 69,401 71,332 68,946


64,82 64,82 65,825 61,917


58,268 58,268 57,668 51,717


79,715 79,715 79,715 79,715


141,5 141,5 141,5 141,5


72,354 72,354 67,033 62,271

Flame tilt (deg)

57,602 57,602 50,022 36,175

View factor (%)

0,022654 0,022654 0,030767 0,043259


46,183 46,183 45,54 44,931




791,19 791,19 771,17 752,23


34,696 34,696 39,254 44,222


1022 1022 1022 1022


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.05.REV FLASHF Case description: onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (08/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)) compared to: onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)) compared to: onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)) Parameters

Inputs

onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))








1,3385E07 1,3385E07 1,3385E07 1,3385E07


543,25 543,25 543,25 543,25


844,73 844,73 844,73 844,73



886,28 886,28 886,28 886,28



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19



Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75




1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results

onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))

onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW))


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


27268 17878 18047 66077

...at time tmem (s)

100 600 700 800




71,494 95 95 186,5


844,73 844,73 844,73 844,73


113,78 494,44 110,81 183,6


155,58 62,589 141,08 381,78


-27,383 -20,493 -22,19 -58,252


13947 22313 12096 48402

...at time tmac (s)

844,73 844,73 844,73 844,73


22341 17878 18047 66077


914,59 21,329 110,81 183,6


155,58 55,219 141,08 381,78


-27,383 -20,493 -22,19 -58,252


429,91 -9,8282 33,214 33,547


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:37:17 UVCE Case description: tank (secondary pump) to compressor - uvce D3 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: tank (secondary pump) to compressor - uvce D3 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool



evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D3 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Parameters

Inputs

tank (secondary pump) to compressor -uvce D3 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass -onboard


tank (secondary pump) to compressor - uvce D3 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard




tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass - onboard

tank (secondary pump) to compressor -uvce E5 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass -onboard

tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass - onboard

tank (secondary pump) to compressor -uvce F2 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosive mass -onboard

tank (secondary pump) to compressor - uvce F2 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosive mass - onboard

tank (secondary pump) to compressor -uvce F2 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosive mass -onboard



tank (secondary pump) to compressor -dispersion D3 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))


tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))




tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

tank (secondary pump) to compressor -dispersion E5 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))

tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

tank (secondary pump) to compressor -dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))

tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

tank (secondary pump) to compressor -dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))


METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


22341 22341 22341 17878 17878 17878 18047 18047 18047 66077 66077 66077


8 8 8 8 8 8 8 8 8 8 8 8

Curve 5 5 5 5 5 5 5 5 5 5 5 5



number (Medium deflagration)













50 50 50 50 50 50 50 50 50 50 50 50


429,91 429,91 429,91 -9,8282 -9,8282 -9,8282 33,214 33,214 33,214 33,547 33,547 33,547


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

tank (secondary pump) to compressor -uvce D3 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosiv


tank (secondary pump) to compressor - uvce D3 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosiv




tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosiv

tank (secondary pump) to compressor -uvce E5 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosiv

tank (secondary pump) to compressor - uvce E5 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosiv

tank (secondary pump) to compressor -uvce F2 LC1 PNEW Z1 (linked to Dense Gas Dispersion: Explosiv

tank (secondary pump) to compressor - uvce F2 LC1 PNEW Z2 (linked to Dense Gas Dispersion: Explosiv

tank (secondary pump) to compressor -uvce F2 LC1 PNEW Z3 (linked to Dense Gas Dispersion: Explosiv



e mass -onboard tank (secondary pump) to compressor -dispersion D3 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))


e mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))




e mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

e mass -onboard tank (secondary pump) to compressor -dispersion E5 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))

e mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

e mass -onboard tank (secondary pump) to compressor -dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))

e mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

e mass -onboard tank (secondary pump) to compressor -dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor -release PNEW)))


1787,3 1787,3 1787,3 1430,2 1430,2 1430,2 1443,8 1443,8 1443,8 5286,1 5286,1 5286,1


89419 89419 89419 71556 71556 71556 72233 72233 72233 2,6447E05

2,6447E05

2,6447E05


206,07 206,07 206,07 201,73 201,73 201,73 201,99 201,99 201,99 206,07 206,07 206,07

Peak dynamic

62,038 62,038 62,038 53,59 53,59 53,59 53,914 53,914 53,914 92,932 92,932 92,932



pressure at Xd (mbar) Pressure impulse at Xd (Pa*s)

2052,5 2052,5 2052,5 1812,2 1812,2 1812,2 1822,4 1822,4 1822,4 3385,4 3385,4 3385,4


199,21 199,21 199,21 179,67 179,67 179,67 180,45 180,45 180,45 328,57 328,57 328,57


68,688 -1E100 -1E100 63,77 -1E100 -1E100 63,971 -1E100 -1E100 98,596 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave















Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed, serious damage to the remaining carrying elements. Damage to windowframes and doors














(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).

(7-15 kPa).















Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40














kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).












Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:36:26 UVCE ED Case description: tank (secondary pump) to compressor - uvce D3 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Parameters

Inputs tank (secondary pump) to compressor - uvce D3

tank (secondary pump) to compressor - uvce D9

tank (secondary pump) to compressor - uvce E5

tank (secondary pump) to compressor - uvce F2



LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))

LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))

LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation -onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))




1,0151 1,0151 1,0151 1,0151


22341 17878 18047 66077


8 8 8 8


50 50 50 50


429,91 -9,8282 33,214 33,547


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

tank (secondary pump) to compressor - uvce D3 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation -

tank (secondary pump) to compressor - uvce D9 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation -

tank (secondary pump) to compressor - uvce E5 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation -

tank (secondary pump) to compressor - uvce F2 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersionF2 PNEW (linked to Pool evaporation -



onboard tank (secondary pump) to compressor -evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))

onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)))

onboard tank (secondary pump) to compressor -evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))

onboard tank (secondary pump) to compressor -evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)))


1787,3 1430,2 1443,8 5286,1


89419 71556 72233 2,6447E05


206,07 201,73 201,99 206,07


62,038 53,59 53,914 92,932


2052,5 1812,2 1822,4 3385,4


199,21 179,67 180,45 328,57


73,049 67,819 68,032 104,86

























framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa). Connections between steel or aluminium ondulated plates have failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).




Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:50:02 PFIRE Case description: B.05 rev D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B.05 rev D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW) compared to: B.05 rev E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW) compared to: B.05 rev F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW) Parameters

Inputs

B.05 rev D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)

B.05 rev D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)

B.05 rev E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)

B.05 rev F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)






1,3385E07 1,3385E07 1,3385E07 1,3385E07


254,91 254,91 254,91 254,91


1800 1800 1800 1800


10000 10000 10000 10000


0 0 0 0




0 0 0 0

Hole diameter (mm)

101,6 101,6 101,6 101,6


1 1 1 1



Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0



Heat radiation level (lowest) for first contour plot

7,3 7,3 7,3 7,3



(kW/m2) Heat radiation level for second contour plot (kW/m2)

9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results

B.05 rev D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)

B.05 rev D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW)

B.05 rev E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)

B.05 rev F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) -onboard tank to compressor - release PNEW)


112,84 112,84 112,84 112,84


0,11465 0,083056 0,10169 0,12194


193,84 189,89 195,74 189,66


177,13 176,96 180,56 172,11


153,44 159,19 159,19 147,33


780 780 780 780


17160 17160 17160 17160


78,846 87,066 80,77 78,846

Flame tilt (deg) 37,614 53,697 45,489 31,201 View factor (%) 0,30773 0,19824 0,26527 0,32729 Atmospheric transmissivity (%)

47,253 48,121 47,462 47,253


814,17 841,32 820,71 814,17


94,407 80,225 90,764 94,407


10000 10000 10000 10000


0 0 0 0


0 0 0 0


0 0 0 0

Weight ratio of 274,4 274,4 274,4 274,4



CO2/chemical (%) Weight ratio of H2O/chemical (%)

224,69 224,69 224,69 224,69




B.06.REV FLASHF Case description: B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (21/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) compared to: B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) compared to: B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) Parameters

Inputs

B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))

B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))








1,3385E07 1,3385E07 1,3385E07 1,3385E07


27,262 40,827 33,206 24,358


1478,9 1542,9 1506,6 1398,3



827,56 939,78 1009 703,08



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0





19 19 19 19

Meteorological data





3 9 5 2



N N N N


0 0 0 0


75 75 75 75


Open water, at least 5 km

Cultivated land Cultivated land Cultivated land


1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results

B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))

B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0




1275,3 0 397,55 3675,8

...at time tmem (s)

1100 0 900 1200


95,313 0 95 267,68


1478,9 0 1506,6 1398,3


276,48 0 0 357,21


49,775 0 0 68,893


-19,305 0 0 -17,529


10725 0 3607,8 15984

...at time tmac (s)

1478,9 0 1506,6 1398,3


1275,3 0 397,55 3675,8


276,48 0 0 357,21


49,775 0 0 68,893


-19,305 0 0 -17,529


118,94 0 0 161,08


0 0 0,011686 0,04733




UVCE Case description: B06 - UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Model: Explosion (Multi Energy model) version: 5.03 (21/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B06 - UVCE D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06- UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06 - UVCE F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Parameters

Inputs

B06 -UVCE D3 Z1 (linked to Dense Gas Dispersion: Explosiv




B06- UVCE D9 Z2 (linked to Dense Gas Dispersion: Explosiv


B06 - UVCE E5 Z1 (linked to Dense Gas Dispersion: Explosiv

B06 -UVCE E5 Z2 (linked to Dense Gas Dispersion: Explosiv

B06 -UVCE E5 Z3 (linked to Dense Gas Dispersion: Explosiv

B06 -UVCE F2 Z1 (linked to Dense Gas Dispersion: Explosiv





e mass -B06_onboard tank (secondary pump) to compressor -dispersion D3 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))






e mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)))

e mass -B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))

e mass -B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))

e mass -B06_onboard tank (secondary pump) to compressor -dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))




METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


1275,3 1275,3 1275,3 0 0 0 397,55 397,55 397,55 3675,8 3675,8 3675,8

Fraction of flammable cloud

8 8 8 8 8 8 8 8 8 8 8 8



confined (%)

Curve number














50 50 50 50 50 50 50 50 50 50 50 50


118,94 118,94 118,94 0 0 0 0 0 0 161,08 161,08 161,08


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

B06 -UVCE D3 Z1 (linked to Dense Gas Dispersion:




B06- UVCE D9 Z2 (linked to Dense Gas Dispersion:


B06 - UVCE E5 Z1 (linked to Dense Gas Dispersion:

B06 -UVCE E5 Z2 (linked to Dense Gas Dispersion:

B06 -UVCE E5 Z3 (linked to Dense Gas Dispersion:

B06 -UVCE F2 Z1 (linked to Dense Gas Dispersion:





Explosive mass -B06_onboard tank (secondary pump) to compressor -dispersion D3 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))






Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)))

Explosive mass -B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))

Explosive mass -B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))

Explosive mass -B06_onboard tank (secondary pump) to compressor -dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release)))




102,03 102,03 102,03 0 0 0 31,804 31,804 31,804 294,07 294,07 294,07


5104,4 5104,4 5104,4 -1E94 -1E94 -1E94 1591,2 1591,2 1591,2 14713 14713 14713


90,116 90,116 90,116 -1E98 -1E98 -1E98 61,505 61,505 61,505 127,83 127,83 127,83

Peak dyna

6,9186 6,9186 6,9186 -1E98 -1E98 -1E98 2,714 2,714 2,714 15,857 15,857 15,857



mic pressure at Xd (mbar) Pressure impulse at Xd (Pa*s)

338,56 338,56 338,56 -1E100 -1E100 -1E100 159,14 159,14 159,14 673,34 673,34 673,34


75,139 75,139 75,139 -1E103 -1E103 -1E103 51,75 51,75 51,75 105,34 105,34 105,34


26,447 -1E100 -1E100 -1E100 -1E100 -1E100 17,933 -1E100 -1E100 37,638 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

*** NOT INITIALIZED

*** NOT INITIALIZED

*** NOT INITIALIZED

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave
























Not habitable without major repair works. Partial roof failures, 25% of all brick walls have failed, serious damage to the remaining carrying element





s. Damage to windowframes and doors (7-15 kPa).





























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 14:57:55 UVCE ED Case description: B06_onboard tank (secondary pump) to compressor - UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions



compared to: B06_onboard tank (secondary pump) to compressor - UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06_onboard tank (secondary pump) to compressor - UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06_onboard tank (secondary pump) to compressor - UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Parameters

Inputs

B06_onboard tank (secondary pump) to compressor - UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor -dispersion D3 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor - release)))


B06_onboard tank (secondary pump) to compressor - UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor - release)))

B06_onboard tank (secondary pump) to compressor - UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor -dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor - release)))




1,0151 1,0151 1,0151 1,0151


1275,3 0 397,55 3675,8


8 8 8 8

Curve number



50 50 50 50


118,94 0 0 161,08


160 160 160 160


0 0 0 0


0 0 0 0

Predefined N N N N



wind direction Wind comes from (North = 0 degrees) (deg)

0 0 0 0

Results



B06_onboard tank (secondary pump) to compressor - UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor -dispersion E5 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor - release)))

B06_onboard tank (secondary pump) to compressor - UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor -dispersion F2 (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor - release)))


102,03 0 31,804 294,07


5104,4 -1E94 1591,2 14713


90,116 -1E98 61,505 127,83


6,9186 -1E98 2,714 15,857


338,56 -1E100 159,14 673,34


75,139 -1E103 51,75 105,34

Dist. from center mass of cloud atthreshold overpressure (m)

28,127 -1E100 19,071 40,028


























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:52:57 PFIRE Case description: B06.REV PFIRE D3 RZ (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B06.REV PFIRE D9 RZ (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) compared to: B06.REV PFIRE E5 RZ (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) compared to: B06.REV PFIRE F2 RZ (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release)) Parameters

Inputs

B06.REV PFIRE D3 RZ (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))


B06.REV PFIRE E5 RZ (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06.REV PFIRE F2 RZ (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))






1,3385E07 1,3385E07 1,3385E07 1,3385E07




27,262 40,827 33,206 24,358


1478,9 1542,9 1506,6 1398,3


1500 1500 1500 1500


0 0 0 0


0 0 0 0

Hole diameter (mm)




Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75

Take protective No No No No



effects of clothing into account X-coordinate of release (m)

0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results



B06.REV PFIRE E5 RZ (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))

B06.REV PFIRE F2 RZ (linked to Pool evaporation -B06_onboard tank (secondary pump) to compressor -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B06.rev_onboard tank to compressor -release))


43,702 43,702 43,702 43,702


0,016398 0,011267 0,013952 0,017793


84,309 82,074 84,474 81,666


76,635 76,577 77,95 73,607


65,297 68,964 68,43 61,726


117 117 117 117

Duration of the 1,144E05 1,144E05 1,144E05 1,144E05



pool fire (s) Heat emission from fire surface (kW/m2)

64,794 74,662 69,177 64,794


45,291 46,484 45,836 45,291


762,39 799,53 779,37 762,39


50,24 39,95 45,199 50,24


1500 1500 1500 1500


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.07 FLASHF Case description: B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (20/06/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) compared to: B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) compared to: B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)) Parameters

Inputs

B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))

B07_pump to ru -dispersion D9 (linked to Pool evaporation -B07_pump to RU -evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))

B07_pump to ru -dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))

B07_pump to ru -dispersion F2 (linked to Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))








3,6387E07 3,6387E07 3,6387E07 3,6387E07


52,281 62,311 51,892 53,861


1068,6 1449,8 1350,9 882,95



662,01 798,37 638,49 701,78



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data



D (Neutral) D (Neutral) D (Neutral) D (Neutral)


3 9 5 2



N N N N




0 0 0 0


75 75 75 75




1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results

B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))

B07_pump to ru -dispersion D9 (linked to Pool evaporation -B07_pump to RU -evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))

B07_pump to ru -dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))

B07_pump to ru -dispersion F2 (linked to Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release))


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


1834,7 190,3 669,32 4050,5


95 95 95 165,8


1068,6 1449,8 1350,9 882,95


191,4 72,008 120,8 261,48


42,652 33,238 37,665 46,537


-16,92 -16,21 -15,976 -17,729

Maximum area of 5968,9 1885,1 3410,2 9829,6



explosive cloud (m2) ...at time tmac (s) 1068,6 1449,8 1350,9 882,95 Explosive mass at time tmac (kg)

1834,7 190,3 669,32 4050,5


191,4 16,206 120,8 261,48


42,652 30,5 37,665 46,537


-16,92 -16,21 -15,976 -17,729


78,783 -8,1074 44,423 113,01


0 0 0 0

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:39:36 UVCE Case description: B07_pump to ru - uvce D3 Z1 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B07_pump to ru - uvce D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce D3 Z3 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce D9 Z1 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce D9 Z3 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 Z3 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))



compared to: B07_pump to ru - uvce F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Parameters

Inputs

B07_pump to ru -uvce D3 Z1 (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -dispersion D3 (linked to Pool evaporation -B07_pump to RU -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru -release)))

B07_pump to ru - uvce D3 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))


B07_pump to ru -uvce D9 Z1 (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -dispersion D9 (linked to Poolevaporation -B07_pump to RU -evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru -release)))

B07_pump to ru - uvce D9 Z2 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))


B07_pump to ru - uvce E5 Z1 (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

B07_pump to ru - uvce E5 Z2 (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru - dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru - release)))

B07_pump to ru - uvce E5 Z3 (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru - dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru - release)))

B07_pump to ru -uvce F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -dispersion F2 (linked to Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release)))




METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


1834,7 1834,7 1834,7 190,3 190,3 190,3 669,32 669,32 669,32 4050,5 4050,5 4050,5




8 8 8 8 8 8 8 8 8 8 8 8

Curve number














50 50 50 50 50 50 50 50 50 50 50 50


78,783 78,783 78,783 -8,1074 -8,1074 -8,1074 44,423 44,423 44,423 113,01 113,01 113,01


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

B07_pump to ru -uvce D3 Z1 (linked to Dense Gas Dispersion:

B07_pump to ru - uvce D3 Z2 (linked to Dense Gas Dispersion:



B07_pump to ru - uvce D9 Z2 (linked to Dense Gas Dispersion:


B07_pump to ru - uvce E5 Z1 (linked to Dense Gas Dispersion: Explosiv



B07_pump to ru -uvce F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -B07_pum





Explosive mass -B07_pump to ru -dispersion D3 (linked to Pool evaporation -B07_pump to RU -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru -release)))

Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))



Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))


e mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

e mass -B07_pump to ru - dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru- release)))

e mass -B07_pump to ru - dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru - release)))

p to ru -dispersion F2 (linked to Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release)))




146,77 146,77 146,77 15,224 15,224 15,224 53,546 53,546 53,546 324,04 324,04 324,04


7343,2 7343,2 7343,2 761,68 761,68 761,68 2679 2679 2679 16212 16212 16212


101,67 101,67 101,67 48,747 48,747 48,747 73,026 73,026 73,026 132,22 132,22 132,22


9,2877 9,2877 9,2877 1,4994 1,4994 1,4994 4,1851 4,1851 4,1851 17,037 17,037 17,037


429,45 429,45 429,45 100,16 100,16 100,16 223,17 223,17 223,17 717,99 717,99 717,99

Positive phase duration at Xd

84,475 84,475 84,475 41,096 41,096 41,096 61,121 61,121 61,121 108,6 108,6 108,6



(ms) Dist. from center mass of cloud at threshold overpressure (m)

29,856 -1E100 -1E100 14,028 -1E100 -1E100 21,333 -1E100 -1E100 38,876 -1E100 -1E100


Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave


Minor damage (Zone D: 3.5 -17 kPa).


























Minor damage. Comparable to a damage due to a storm; wooden walls fail, breaka






Minor damage. Comparable to a damage due to a storm; wooden walls fail, breakage of windows (7-10








ge of windows (7-10 kPa).



kPa). kPa). kPa).














Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:30:38 UVCE ED Case description: B07_pump to ru - uvce D3 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B07_pump to ru - uvce D9 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce F2 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Parameters

Inputs

B07_pump to ru - uvce D3 ED (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -

B07_pump to ru - uvce D9 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru -

B07_pump to ru - uvce E5 ED (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -

B07_pump to ru - uvce F2 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru -dispersion F2 (linked to



dispersion D3 (linked to Pool evaporation -B07_pump to RU -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release)))

dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru -release)))




1,0151 1,0151 1,0151 1,0151


1834,7 190,3 669,32 4050,5


8 8 8 8

Curve number 5 (Medium deflagration)


5 (Medium deflagration) 5 (Medium deflagration)


50 50 50 50


78,783 -8,1074 44,423 113,01


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

B07_pump to ru - uvce D3 ED (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -dispersion D3 (linked to Pool evaporation -B07_pump to RU -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B07_pump to ru -release)))

B07_pump to ru - uvce D9 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

B07_pump to ru - uvce E5 ED (linked to Dense Gas Dispersion: Explosive mass -B07_pump to ru -dispersion E5 (linked to Pool evaporation -B07_pump to RU -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)))

B07_pump to ru - uvce F2 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru -dispersion F2 (linked to Pool evaporation -B07_pump to RU -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru -release)))


146,77 15,224 53,546 324,04


7343,2 761,68 2679 16212

Peak 101,67 48,747 73,026 132,22



overpressure at Xd (mbar) Peak dynamic pressure at Xd (mbar)

9,2877 1,4994 4,1851 17,037


429,45 100,16 223,17 717,99


84,475 41,096 61,121 108,6


31,752 14,919 22,688 41,344























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 9:55:57 PFIRE Case description: B07_pump to RU - PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B07_pump to RU - PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)



compared to: B07_pump to RU - PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) compared to: B07_pump to RU - PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release) Parameters

Inputs

B07_pump to RU -PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)


B07_pump to RU -PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)

B07_pump to RU -PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)






3,6387E07 3,6387E07 3,6387E07 3,6387E07


539,25 539,25 539,25 539,25


1800 1800 1800 1800


1500 1500 1500 1500


0 0 0 0


0 0 0 0

Hole diameter (mm)

152,4 152,4 152,4 152,4


1 1 1 1



Pool thickness (mm)


19 19 19 19

Pool burning rateCalculate/Default Calculate/Default Calculate/Default Calculate/Default Value of pool burning rate (kg/m2*s)


35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75

Amount of CO2 0,03 0,03 0,03 0,03



in atmosphere (%) Distance from the centre of the pool (m)

1000 1000 1000 1000


75 75 75 75


No No No No

X-coordinate ofrelease (m)

0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 7,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4


Results



B07_pump to RU -PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)

B07_pump to RU -PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release)


43,702 43,702 43,702 43,702


0,016398 0,011267 0,013952 0,017793


84,309 82,074 84,474 81,666


76,635 76,577 77,95 73,607


65,297 68,964 68,43 61,726


117 117 117 117


3,11E05 3,11E05 3,11E05 3,11E05




64,794 74,662 69,177 64,794


45,291 46,484 45,836 45,291


762,39 799,53 779,37 762,39


50,24 39,95 45,199 50,24

Calculated poolsurface area (m2)

1500 1500 1500 1500


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69




B.08.REV JFIRE Case description: B08_rev_vaporizer - JFIRE D3 pnew Model: Gas Jet Fire (Chamberlain model) version: 5.12 (04/11/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B08_rev_vaporizer - JFIRE D9 pnew compared to: B08_rev_vaporizer - JFIRE E5 pnew compared to: B08_rev_vaporizer - JFIRE F2 pnew Parameters

Inputs B08_rev_vaporizer - JFIRE D3 pnew

B08_rev_vaporizer -JFIRE D9 pnew

B08_rev_vaporizer -JFIRE E5 pnew

B08_rev_vaporizer -JFIRE F2 pnew



Type of release Release through hole in vessel

Release through hole in vessel



Pipeline length (m) Pipeline diameter (mm) Pipeline roughness (mm)

Hole diameter (inch) 1,5 1,5 1,5 1,5 Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges Discharge coefficient (-)

1 1 1 1

Initial temperature in vessel (°C)

-150 -150 -150 -150


45 45 45 45


0 0 0 0


1 1 1 1


3 9 5 2


19 19 19 19


75 75 75 75

Flame temperature (K) 1500 1500 1500 1500 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results B08_rev_vaporizer - JFIRE D3 pnew

B08_rev_vaporizer -JFIRE D9 pnew

B08_rev_vaporizer -JFIRE E5 pnew

B08_rev_vaporizer -JFIRE F2 pnew


43,226 43,226 43,226 43,226

Type of flow of the jet Choked flow Choked flow Choked flow Choked flow



Exit velocity of expanding jet (m/s)

559,36 559,36 559,36 559,36


0 0 0 0


15,299 11,979 13,288 17,095


0,15197 0,14306 0,14784 0,16926


22,011 19,946 20,219 23,834


61,195 47,915 53,152 68,378


0 0 0 0

Surface area of frustum(m2)

2544,7 1856,4 2051,7 3062,6


2323,3 1670,5 1863,4 2804,4


134,49 187,05 167,68 111,42


134,49 187,05 167,68 111,42


75,183 74,885 74,992 75,355


5,7851 2,278 3,0107 13,672

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:40:29 FLASHF Case description: B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (04/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew) compared to: B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew) compared to: B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew) Parameters

Inputs

B08_rev_vaporizer -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D3 pnew)

B08_rev_vaporizer -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D9 pnew)

B08_rev_vaporizer -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE E5 pnew)

B08_rev_vaporizer -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE F2 pnew)



Type of release Semi-continuous Semi-continuous Semi-continuous Semi-continuous Total mass released (kg)


12,828 12,828 12,828 12,828


120 120 120 120




0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


19 19 19 19

Meteorological data





3 9 5 2


35 35 35 35


Mixing height (m)

Stand. dev. of turbulent velocity in vertical direction (m/s)








N N N N


0 0 0 0


120 120 120 120


20 20 20 20


0,1 0,1 0,1 0,1


Low Low Low Low

Results

B08_rev_vaporizer -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -

B08_rev_vaporizer -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -

B08_rev_vaporizer -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -

B08_rev_vaporizer -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -



B08_rev_vaporizer -JFIRE D3 pnew)

B08_rev_vaporizer -JFIRE D9 pnew)

B08_rev_vaporizer -JFIRE E5 pnew)

B08_rev_vaporizer -JFIRE F2 pnew)


293,84 49,962 199,79 1090,1


8,3 5,1 6 7,8


122,04 62,01 138,6 248,4


8,2879 4,4968 6,9321 12,274


0,01 0,01 0,01 0,01


294,14 49,962 199,8 1119,6

...at time tmem (s)

120 120 120 125


39,738 9,517 28,237 117,54


121,44 120,5 120,95 141,82


122,04 62,01 138,6 248,4


8,2879 4,4968 6,9321 12,274


0,01 0,01 0,01 0,01


795,2 220,25 751,72 2712

...at time tmac (s)

120 120 120 175


294,14 49,962 199,8 853,01


122,04 62,01 138,6 244,8


8,2879 4,4968 6,9321 13,152


0,01 0,01 0,01 91,261


61,03 31,015 69,31 213,66

Inverse Monin-0 0 0,014548 0,060302



Obukhov length (1/L) used (1/m) Mixing height used (m)

500 500 247,92 62,735


0,63265 1,8979 0,88561 0,23504


0,43475 1,3042 0,60594 0,16082

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:40:55 UVCE Case description: B08_rev_vaporizer - uvce D3 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B08_rev_vaporizer - uvce D3 pNew Z2 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew)) compared to: B08_rev_vaporizer - uvce D3 pNew Z3 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew)) compared to: B08_rev_vaporizer - uvce D9 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew)) compared to: B08_rev_vaporizer - uvce D9 pNew Z2 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew)) compared to: B08_rev_vaporizer - uvce D9 pNew Z3 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew)) compared to: B08_rev_vaporizer - uvce E5 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew)) compared to: B08_rev_vaporizer - uvce E5 pNew Z2 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew)) compared to: B08_rev_vaporizer - uvce E5 pNew Z3 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew)) compared to: B08_rev_vaporizer - uvce F2 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew)) compared to: B08_rev_vaporizer - uvce F2 pNew Z2 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew)) compared to: B08_rev_vaporizer - uvce F2 pNew Z3 (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew)) Parameters

Inputs B08_rev_vaporizer - uvce

B08_rev_vaporizer - uvce













D3 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D3 pnew))






E5 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE E5 pnew))



F2 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE F2 pnew))




METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


294,14 294,14 294,14 49,962 49,962 49,962 199,8 199,8 199,8 853,01 853,01 853,01


8 8 8 8 8 8 8 8 8 8 8 8

Curve number













Distance from release (Xd)

50 50 50 50 50 50 100 100 100 100 100 100



(m) Offset between release point and cloud centre (m)

61,03 61,03 61,03 31,015 31,015 31,015 69,31 69,31 69,31 213,66 213,66 213,66


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0

Results

B08_rev_vaporizer - uvce D3 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersi






B08_rev_vaporizer - uvce E5 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersi



B08_rev_vaporizer - uvce F2 pNew Z1 (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersi





on D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D3 pnew))



on D9 pNew (linked to GasJet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D9 pnew))



on E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE E5 pnew))



on F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE F2 pnew))




23,531 23,531 23,531 3,997 3,997 3,997 15,984 15,984 15,984 68,241 68,241 68,241


1177,3 1177,3 1177,3 199,97 199,97 199,97 799,7 799,7 799,7 3414,1 3414,1 3414,1


55,687 55,687 55,687 30,152 30,152 30,152 24,38 24,38 24,38 38,871 38,871 38,871


2,1376 2,1376 2,1376 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


130,6 130,6 130,6 39,904 39,904 39,904 51,326 51,326 51,326 132,15 132,15 132,15


46,905 46,905 46,905 26,469 26,469 26,469 42,105 42,105 42,105 67,994 67,994 67,994

Dist. from center mass of

16,219 -1E100 -1E100 8,9824 -1E100 -1E100 14,258 -1E100 -1E100 23,129 -1E100 -1E100



cloud at threshold overpressure (m) Blast-wave shape at Xd

Pressure wave

Pressure wave

Pressure wave

Shock Wave

Shock Wave

Shock Wave

Shock Wave

Shock Wave

Shock Wave

Pressure wave

Pressure wave

Pressure wave













































No damage or veryminor damage








Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:21:43 UVCE ED Case description: B08_rev_vaporizer - uvce D3 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew))



Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B08_rev_vaporizer - uvce D9 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew)) compared to: B08_rev_vaporizer - uvce E5 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew)) compared to: B08_rev_vaporizer - uvce F2 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew)) Parameters

Inputs

B08_rev_vaporizer -uvce D3 pNew ED (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D3 pnew))

B08_rev_vaporizer -uvce D9 pNew ED (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D9 pnew))

B08_rev_vaporizer -uvce E5 pNew ED (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE E5 pnew))

B08_rev_vaporizer -uvce F2 pNew ED (linked to Neutral Gas Dispersion: Explosive mass -B08_rev_vaporizer -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE F2 pnew))




1,0151 1,0151 1,0151 1,0151


294,14 49,962 199,8 853,01


8 8 8 8


50 50 100 100


61,03 31,015 69,31 213,66


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

B08_rev_vaporizer -uvce D3 pNew ED (linked to Neutral Gas Dispersion: Explosive

B08_rev_vaporizer -uvce D9 pNew ED (linked to Neutral Gas Dispersion: Explosive

B08_rev_vaporizer -uvce E5 pNew ED (linked to Neutral Gas Dispersion: Explosive

B08_rev_vaporizer -uvce F2 pNew ED (linked to Neutral Gas Dispersion: Explosive



mass -B08_rev_vaporizer -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D3 pnew))

mass -B08_rev_vaporizer -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE D9 pnew))

mass -B08_rev_vaporizer -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE E5 pnew))

mass -B08_rev_vaporizer -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B08_rev_vaporizer -JFIRE F2 pnew))


23,531 3,997 15,984 68,241


1177,3 199,97 799,7 3414,1


55,687 30,152 24,38 38,871


2,1376 1,0151 1,0151 1,0151


130,6 39,904 51,326 132,15


46,905 26,469 42,105 67,994


17,249 9,5527 15,163 24,598


Pressure wave Shock Wave Shock Wave Pressure wave





















Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 10:00:13 PFIRE



NO THERMAL RADIATION EFFECTS



B.09.REV JFIRE Case description: B09_RU to ME - JFIRE D3 pNew Model: Gas Jet Fire (Chamberlain model) version: 5.12 (11/11/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B09_RU to ME - JFIRE D9 pNew compared to: B09_RU to ME - JFIRE E5 pNew compared to: B09_RU to ME - JFIRE F2 pNew Parameters

Inputs B09_RU to ME -JFIRE D3 pNew

B09_RU to ME - JFIRE D9 pNew

B09_RU to ME -JFIRE E5 pNew

B09_RU to ME -JFIRE F2 pNew






Pipeline length (m) 26,5 26,5 26,5 26,5 Pipeline diameter (inch) 10 10 10 10 Pipeline roughness (mm) 0,045 0,045 0,045 0,045 Hole diameter (inch) 10 10 10 10 Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges Discharge coefficient (-) 1 1 1 1 Initial temperature in vessel (°C)

-5 -5 -5 -5


45 45 45 45


0 0 0 0


0 0 0 0


3 9 5 2


75 75 75 75

Flame temperature (K) 1500 1500 1500 1500 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100

X-coordinate of release (m) 0 0 0 0 Y-coordinate of release (m) 0 0 0 0 Predefined wind direction N N N N Wind comes from (North = 0 degrees) (deg)

0 0 0 0

Results B09_RU to ME -JFIRE D3 pNew

B09_RU to ME - JFIRE D9 pNew

B09_RU to ME -JFIRE E5 pNew

B09_RU to ME -JFIRE F2 pNew

Initial source strength (kg/s) 348,37 348,37 348,37 348,37 Type of flow of the jet Choked flow Choked flow Choked flow Choked flow Exit velocity of expanding jet (m/s)

832,07 832,07 832,07 832,07


0 0 0 0


0,57101 0,51213 0,52697 0,96462


49,361 43,277 44,697 53,924




141,54 110,82 122,94 158,15


0 0 0 0


13179 9234,4 10442 16110


12080 8375,7 9536,1 14819


179,33 258,64 227,17 146,19


179,33 258,64 227,17 146,19


77,477 76,611 76,901 78,049

View factor (%) 100 100 100 100 Heat radiation at Xd (kW/m2)

179,33 258,64 227,17 146,19

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:41:40 FLASHF Case description: B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (11/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew) compared to: B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew) compared to: B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew) Parameters

Inputs

B09_RU to ME -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE D3 pNew)


B09_RU to ME -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE E5 pNew)

B09_RU to ME -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE F2 pNew)



Type of release Semi-continuous Semi-continuous Semi-continuous Semi-continuous Total mass released (kg)


348,37 348,37 348,37 348,37


120 120 120 120


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0

Length source in 0 0 0 0



crosswind (y) direction (m) Length source in vertical (z) direction (m)

0 0 0 0


19 19 19 19

Meteorological data Pasquill Pasquill Pasquill Pasquill Pasquill stability class

D (Neutral) D (Neutral) E (Stable) D (Neutral)


3 9 5 2


51 51 51 51










N N N N


0 0 0 0


120 120 120 120


20 20 20 20


0,1 0,1 0,1 0,1


Low Low Low Low

Results



B09_RU to ME -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE E5 pNew)

B09_RU to ME -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE F2 pNew)


30561 10175 28928 27676


32,8 22,1 24,8 31,7


390,78 470,88 617,8 278,88


43,62 28,07 41,718 41,753

Offset between release location and LEL at time t

0,01 0,01 0,01 0,01



(m) Maximum explosive mass (kg)

32805 10173 29915 34754


123,58 52,018 117,6 143,32


161,56 120 142,56 216,47


390,78 470,88 617,8 278,88


43,62 28,07 41,718 41,753


0,01 0,01 0,01 0,01


16799 10305 22514 15319

...at time tmac (s) 200 120 175 300 Explosive mass at time tmac (kg)

25245 10173 22558 24903


400,82 470,88 602,98 322,08


50,144 28,07 44,174 59,21


198,91 0,01 227,69 305,26


399,32 235,45 529,18 466,3


0 0 0,014548 0


500 500 212,99 393,44

Stand. dev. of turbulent velocity invert. direction used (m/s)

0,63265 1,8979 0,88561 0,42177


0,43475 1,3042 0,60594 0,28983

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010



Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:42:05 UVCE Case description: B09_RU to ME - UVCE D3 Z1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew)) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B09_RU to ME - UVCE D3 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew)) compared to: B09_RU to ME - UVCE D3 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew)) compared to: B09_RU to ME - UVCE D9 Z1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew)) compared to: B09_RU to ME - UVCE D9 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew)) compared to: B09_RU to ME - UVCE D9 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew)) compared to: B09_RU to ME - UVCE E5 Z1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew)) compared to: B09_RU to ME - UVCE E5 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew)) compared to: B09_RU to ME - UVCE E5 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew)) compared to: B09_RU to ME - UVCE F2 Z1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew)) compared to: B09_RU to ME - UVCE F2 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew)) compared to: B09_RU to ME - UVCE F2 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew)) Parameters

Inputs

B09_RU to ME -UVCE D3 Z1 (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME -dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME -JFIRE D3 pNew))


B09_RU to ME - UVCE D3 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew))




B09_RU to ME - UVCE E5 Z1 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew))

B09_RU to ME -UVCE E5 Z2 (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME -JFIRE E5 pNew))


B09_RU to ME -UVCE F2 Z1 (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME -dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME -JFIRE F2 pNew))

B09_RU to ME - UVCE F2 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew))



METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)




1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151 1,0151


25245 25245 25245 10173 10173 10173 22558 22558 22558 24903 24903 24903


8 8 8 8 8 8 8 8 8 8 8 8

Curve number














50 50 50 50 50 50 100 100 100 100 100 100


399,32 399,32 399,32 235,45 235,45 235,45 529,18 529,18 529,18 466,3 466,3 466,3


170 360 900 170 360 900 170 360 900 170 360 900


0 0 0 0 0 0 0 0 0 0 0 0


0 0 0 0 0 0 0 0 0 0 0 0




0 0 0 0 0 0 0 0 0 0 0 0



Results



B09_RU to ME - UVCE D3 Z3 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew))





B09_RU to ME -UVCE E5 Z2 (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME -dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME -JFIRE E5 pNew))



B09_RU to ME - UVCE F2 Z2 (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew))



2019,6 2019,6 2019,6 813,87 813,87 813,87 1804,6 1804,6 1804,6 1992,3 1992,3 1992,3


1,0104E05

1,0104E05

1,0104E05

40719 40719 40719 90286 90286 90286 99675 99675 99675


206,07 206,07 206,07 179,26 179,26 179,26 116,86 116,86 116,86 120,84 120,84 120,84


67,816 67,816 67,816 35,059 35,059 35,059 13 13 13 14,011 14,011 14,011


2172 2172 2172 1311,6 1311,6 1311,6 1132,7 1132,7 1132,7 1208,3 1208,3 1208,3


210,81 210,81 210,81 146,33 146,33 146,33 193,87 193,87 193,87 199,98 199,98 199,98

Dist. from

71,543 -1E100 -1E100 52,845 -1E100 -1E100 68,909 -1E100 -1E100 71,219 -1E100 -1E100



center mass of cloud at threshold overpressure (m) Blast-wave shape at Xd

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave

Pressure wave
















Not habitable without major repair works. Partial roof failures, 25% of all brickwalls have failed, serious damage to the remaining carrying elements. Damage to windowframes and doors (7-15 kPa).












Moderate to minor damage. Deformed walls and doors; failure of joints. Doors and window






Minor damage. Comparable to a damage due to a storm; wooden walls fail, breakage of windows








frames have failed. Wall covering has fallen down (15 kPa).






(7-10 kPa).

(7-10 kPa).

(7-10 kPa).

(7-10 kPa).

(7-10 kPa).

(7-10 kPa).


Collapse of steel frames and displacement of foundation (20 kPa). Industrial steel self-framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30 kPa). Slight deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down (20-40 kPa). Walls made of concrete blocks have collapsed (15-20). Minor damage to steel frames (8-10 kPa).

















Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 11:13:33 UVCE ED Case description: B09_RU to ME - UVCE D3 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B09_RU to ME - UVCE D9 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew)) compared to: B09_RU to ME - UVCE E5 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew)) compared to: B09_RU to ME - UVCE F2 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew)) Parameters

Inputs

B09_RU to ME - UVCE D3 ED (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE D3 pNew))

B09_RU to ME - UVCE D9 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE D9 pNew))

B09_RU to ME -UVCE E5 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew))

B09_RU to ME -UVCE F2 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew))




1,0151 1,0151 1,0151 1,0151


25245 10173 22558 24903


8 8 8 8

Curve number 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration)

5 (Mediumdeflagration)




50 50 100 100


399,32 235,45 529,18 466,3


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results

B09_RU to ME - UVCE D3 ED (linked to Neutral Gas Dispersion: Explosive mass -B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE D3 pNew))

B09_RU to ME - UVCE D9 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME -dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) -B09_RU to ME - JFIRE D9 pNew))

B09_RU to ME -UVCE E5 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew))

B09_RU to ME -UVCE F2 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew))


2019,6 813,87 1804,6 1992,3


1,0104E05 40719 90286 99675


206,07 179,26 116,86 120,84


67,816 35,059 13 14,011


2172 1311,6 1132,7 1208,3


210,81 146,33 193,87 199,98


76,086 56,2 73,284 75,741

























Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 15/11/2013 10:03:46 PFIRE NO THERMAL RADIATION EFFECTS



B.10 JFIRE Case description: B10_tank to BOC - JFIRE D3 not realistic Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/06/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B10_tank to BOC - JFIRE D9 not realistic compared to: B10_tank to BOC - JFIRE E5 not realistic compared to: B10_tank to BOC - JFIRE F2 not realistic Parameters

Inputs B10_tank to BOC -JFIRE D3 not realistic

B10_tank to BOC - JFIRE D9 not realistic

B10_tank to BOC -JFIRE E5 not realistic

B10_tank to BOC -JFIRE F2 not realistic







19 19 19 19


15 15 15 15


0 0 0 0


40 40 40 40


3 9 5 2


75 75 75 75

Flame temperature (°C) 1500 1500 1500 1500 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


0 0 0 0

Results B10_tank to BOC -JFIRE D3 not realistic


B10_tank to BOC -JFIRE E5 not realistic

B10_tank to BOC -JFIRE F2 not realistic


777,61 777,61 777,61 777,61


1,1355 5,7196 2,3395 0,66464


0,043405 0,041467 0,042632 0,047204




4,4851 3,9538 4,0705 4,8931


13,022 10,508 11,431 14,471


0,924 4,7943 1,9238 0,53788


109,77 79,355 88,005 132,66


100,68 72,212 80,496 121,88


94,649 131,97 118,38 78,188


94,649 131,97 118,38 78,188


78,093 78,044 78,065 78,118


0,03786 0,031165 0,035345 0,039616

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:42:44 UVCE NO MASS IN EXPLOSIVE RANGE UVCE ED NO MASS IN EXPLOSIVE RANGE PFIRE NO THERMAL RADIATION EFFECTS B.11 JFIRE Case description: B11_tank to BOC - JFIRE D3 not realistic Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/06/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B11_tank to BOC - JFIRE D9 not realistic compared to: B11_tank to BOC - JFIRE E5 not realistic compared to: B11_tank to BOC - JFIRE F2 not realistic Parameters

Inputs B11_tank to BOC - JFIRE D3 not realistic


B11_tank to BOC - JFIRE E5 not realistic

B11_tank to BOC - JFIRE F2 not realistic

B11_tank to BOC - JFIRE D3 not realistic copy


METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)






Pipeline length (m) 25000 25000 25000 25000 25000 Pipeline diameter (inch) 6 6 6 6 6 Pipeline roughness (mm)

0,045 0,045 0,045 0,045 0,045

Hole diameter (inch) 6 6 6 6 6 Hole rounding Rounded edges Rounded edges Rounded edges Rounded edges Rounded edges Discharge coefficient (-) 1 1 1 1 1 Initial temperature in vessel (°C)

19 19 19 19 19

Initial (absolute) 15 15 15 15 38



pressure in vessel (bar) Outflow angle in XZ plane (0°=horizontal; 90°=vertical) (deg)

0 0 0 0 0


40 40 40 40 40


3 9 5 2 3


19 19 19 19 19


75 75 75 75 75

Flame temperature (°C) 1500 1500 1500 1500 1500 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03 0,03


0 0 0 0 0


100 100 100 100 100


0 0 0 0 0


0 0 0 0 0


N N N N N


0 0 0 0 0

Results B11_tank to BOC - JFIRE D3 not realistic


B11_tank to BOC - JFIRE E5 not realistic

B11_tank to BOC - JFIRE F2 not realistic

B11_tank to BOC - JFIRE D3 not realistic copy


1,4993 1,4993 1,4993 1,4993 3,9424

Type of flow of the jet Choked flow Choked flow Choked flow Choked flow Choked flow Exit velocity of expanding jet (m/s)

777,61 777,61 777,61 777,61 859,76


1,1355 5,7196 2,3395 0,66464 0,53242


2,9808 2,0302 2,4702 3,4104 4,5221


0,043405 0,041467 0,042632 0,047204 0,060633


4,4851 3,9538 4,0705 4,8931 6,7133


13,022 10,508 11,431 14,471 19,592


0,924 4,7943 1,9238 0,53788 0,43257


109,77 79,355 88,005 132,66 246,85


100,68 72,212 80,496 121,88 226,48


94,649 131,97 118,38 78,188 107,18


94,649 131,97 118,38 78,188 107,18


78,093 78,044 78,065 78,118 78,312

View factor (%) 0,051111 0,030187 0,038164 0,064714 0,13592 Heat radiation at Xd (kW/m2)

0,03786 0,031165 0,035345 0,039616 0,11437



Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:43:32 UVCE NO MASS IN EXPLOSIVE RANGE UVCE ED NO MASS IN EXPLOSIVE RANGE PFIRE NO THERMAL RADIATION EFFECTS



B.12 JFIRE Case description: B12_BOC to Liquifier - modified not realistic D3 Model: Gas Jet Fire (Chamberlain model) version: 5.12 (25/06/2013) Reference: Chamberlain, G.A., Development in design methods for predicting thermal radiation from flares~Chem. Eng. Res. Des. Vol.65 July 1987 pagina 299 - 309~ compared to: B12_BOC to Liquifier - modified not realistic D9 compared to: B12_BOC to Liquifier - modified not realistic E5 compared to: B12_BOC to Liquifier - modified not realistic F2 Parameters

Inputs B12_BOC to Liquifier - modified not realistic D3

B12_BOC to Liquifier - modified not realistic D9

B12_BOC to Liquifier - modified not realistic E5

B12_BOC to Liquifier - modified not realistic F2







19 19 19 19


15 15 15 15


0 0 0 0


40 40 40 40


3 9 5 2


75 75 75 75

Flame temperature (°C) 1500 1500 1500 1500 Amount of CO2 in atmosphere (%)

0,03 0,03 0,03 0,03


0 0 0 0


100 100 100 100


0 0 0 0

Results B12_BOC to Liquifier - modified not realistic D3

B12_BOC to Liquifier - modified not realistic D9

B12_BOC to Liquifier - modified not realistic E5

B12_BOC to Liquifier - modified not realistic F2


777,61 777,61 777,61 777,61


1,1355 5,7196 2,3395 0,66464


2,9808 2,0302 2,4702 3,4104

Width of frustum base (W1) 0,043405 0,041467 0,042632 0,047204



(m) Width of frustum tip (W2) (m)

4,4851 3,9538 4,0705 4,8931


13,022 10,508 11,431 14,471


0,924 4,7943 1,9238 0,53788


109,77 79,355 88,005 132,66


100,68 72,212 80,496 121,88


94,649 131,97 118,38 78,188


94,649 131,97 118,38 78,188


78,093 78,044 78,065 78,118


0,03786 0,031165 0,035345 0,039616

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:58:36 FLASHF Case description: B12_BOC to Liquifier - modified not realistic DISPERSION D3 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) Model: Neutral Gas Dispersion: Explosive mass version: 5.14 (25/06/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Chapter 4 compared to: B12_BOC to Liquifier - modified not realistic DISPERSION D9 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) compared to: B12_BOC to Liquifier - modified not realistic DISPERSION E5 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) compared to: B12_BOC to Liquifier - modified not realistic DISPERSION F2 (linked to Gas Jet Fire (Chamberlain model) - B12_BOC to Liquifier - modified not realistic D3) Parameters

Inputs

B12_BOC to Liquifier -modified not realistic DISPERSION D3 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -modified not realistic D3)


B12_BOC to Liquifier -modified not realistic DISPERSION E5 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -modified not realistic D3)

B12_BOC to Liquifier -modified not realistic DISPERSION F2 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -modified not realistic D3)



Type of release Continuous Continuous Continuous Continuous Total mass released (kg)


1,4993 1,4993 1,4993 1,4993



0 0 0 0


0 0 0 0

Z-coordinate (height) of release

0 0 0 0



(m) Length source in wind (x) direction (m)

0 0 0 0


0 0 0 0


0 0 0 0


19 19 19 19

Meteorological data





3 9 5 2


51 51 51 51










N N N N


0 0 0 0



20 20 20 20


0,1 0,1 0,1 0,1


Results



B12_BOC to Liquifier -modified not realistic DISPERSION E5 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -modified not realistic D3)

B12_BOC to Liquifier -modified not realistic DISPERSION F2 (linked to Gas Jet Fire (Chamberlain model) -B12_BOC to Liquifier -modified not realistic D3)


9,1894 1,555 6,0631 47,811


3,2 2 2,4 3,3

Length of cloud 32,44 16,38 35,9 114,1



(between LEL) at time t (m) Width of cloud (between LEL) at time t (m)

2,5029 1,351 2,0542 3,7754


0,01 0,01 0,01 0,01


9,1894 1,555 6,0631 47,811


0 0 0 0


0 0 0 0


32,44 16,38 35,9 114,1


2,5029 1,351 2,0542 3,7754


0,01 0,01 0,01 0,01


64,445 17,673 58,213 336,1


9,1894 1,555 6,0631 47,811


32,44 16,38 35,9 114,1


2,5029 1,351 2,0542 3,7754


0,01 0,01 0,01 0,01


16,23 8,2 17,96 57,06


0 0 0,014548 0,060302


500 500 212,99 53,896


0,63265 1,8979 0,88561 0,23504

Stand. dev. of turbulent velocity

0,43475 1,3042 0,60594 0,16082



in horiz. direction used (m/s) Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:59:05 UVCE NO MASS IN EXPLOSIVE RANGE UVCE ED NO MASS IN EXPLOSIVE RANGE PFIRE NO THERMAL RADIATION EFFECTS



B.13 FLASHF Case description: B13_liquifier to tank - dispersion D3 (linked to Pool evaporation - B13_liquifier to tank - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) Model: Dense Gas Dispersion: Explosive mass version: 5.13 (07/11/2013) Reference: Yellow Book 3rd edition 1997 chapter 4; Ermak, D.L. User manual for SLAB Lawrence Livermore National Laboratory, June 1990 compared to: B13_liquifier to tank - dispersion D9 (linked to Pool evaporation - B13_liquifier to tank - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) compared to: B13_liquifier to tank - dispersion E5 (linked to Pool evaporation - B13_liquifier to tank - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) compared to: B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)) Parameters

Inputs

B13_liquifier to tank -dispersion D3 (linked to Pool evaporation -B13_liquifier to tank -evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank -release))


B13_liquifier to tank -dispersion E5 (linked to Pool evaporation -B13_liquifier to tank -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank -release))

B13_liquifier to tank -dispersion F2 (linked to Pool evaporation -B13_liquifier to tank -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank -release))








13479 13479 13479 13479


8,6222 8,8372 8,7172 8,561


1530,9 1512,8 1523,1 1536



650,59 485,83 580,21 698,49



-161,49 -161,49 -161,49 -161,49


0 0 0 0


0 0 0 0



19 19 19 19

Meteorological data





3 9 5 2



N N N N




0 0 0 0


75 75 75 75




1800 1800 1800 1800


20 20 20 20


Low Low Low Low

Results



B13_liquifier to tank -dispersion E5 (linked to Pool evaporation -B13_liquifier to tank -evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank -release))

B13_liquifier to tank -dispersion F2 (linked to Pool evaporation -B13_liquifier to tank -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank -release))


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 0


0 0 0 460,15

...at time tmem (s)

0 0 0 1500


0 0 0 105,22


0 0 0 1536


0 0 0 127,82


0 0 0 42,894


0 0 0 -15,957




0 0 0 4607


0 0 0 460,15


0 0 0 127,82


0 0 0 42,894


0 0 0 -15,957


0 0 0 47,953


0 0 0,011686 0,04733

Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 21/11/2013 10:59:45 UVCE Case description: B13_liquifier to tank - uvce F2 Z1 (linked to Dense Gas Dispersion: Explosive mass - B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release))) Model: Explosion (Multi Energy model) version: 5.03 (22/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B13_liquifier to tank - uvce F2 Z2 (linked to Dense Gas Dispersion: Explosive mass - B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release))) compared to: B13_liquifier to tank - uvce F2 Z3 (linked to Dense Gas Dispersion: Explosive mass - B13_liquifier to tank - dispersion F2 (linked to Pool evaporation - B13_liquifier to tank - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release))) Parameters

Inputs

B13_liquifier to tank - uvce F2 Z1 (linked to Dense Gas Dispersion: Explosive mass -B13_liquifier to tank - dispersion F2 (linked to Pool evaporation -B13_liquifier to tank -evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) -B13_liquifier to tank - release)))




METHANE (DIPPR) METHANE (DIPPR) METHANE (DIPPR)


1,0151 1,0151 1,0151


460,15 460,15 460,15

Fraction of 8 8 8



flammable cloud confined (%) Curve number 5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration) Distance from release (Xd) (m)

50 50 50


47,953 47,953 47,953


170 360 900


0 0 0


0 0 0


N N N


0 0 0

Results





36,812 36,812 36,812


1841,7 1841,7 1841,7


64,561 64,561 64,561


3,0738 3,0738 3,0738


175,22 175,22 175,22


54,279 54,279 54,279


18,828 -1E100 -1E100


Pressure wave Pressure wave Pressure wave






Habitable after relatively easy repairs. Minor structural





damage (3 kPa). damage (3 kPa). damage (3 kPa). Damage to typical American-style houses at Xd








Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 10:47:32 PFIRE Case description: B13_liquifier to tank - PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) Model: Pool fire version: 5.11 (21/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.4 compared to: B13_liquifier to tank - PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) compared to: B13_liquifier to tank - PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release) Parameters

Inputs

B13_liquifier to tank -PFIRE D3 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)

B13_liquifier to tank -PFIRE D9 RZ (linked to Liquefied Gas Bottom Discharge (TPDISmodel) - B13_liquifier to tank - release)

B13_liquifier to tank -PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)

B13_liquifier to tank -PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)






13479 13479 13479 13479


9,1505 9,1505 9,1505 9,1505


1473 1473 1473 1473


2206 2206 2206 2206


0 0 0 0


0 0 0 0

Hole diameter (mm)

101,6 101,6 101,6 101,6


1 1 1 1


Cross-sectional



area of the tank (m2) Pool thickness (mm)


19 19 19 19

Pool burning rate




35 35 35 35



3 9 5 2


19 19 19 19


75 75 75 75


0,03 0,03 0,03 0,03


1000 1000 1000 1000


75 75 75 75


No No No No


0 0 0 0


0 0 0 0


N N N N


0 0 0 0




7,3 6,3 7,3 7,3


9,3 9,3 9,3 9,3


13,4 13,4 13,4 13,4

Percentage of mortality for contour



calculations (%)

Results



B13_liquifier to tank -PFIRE E5 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)

B13_liquifier to tank -PFIRE F2 RZ (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B13_liquifier to tank - release)


52,998 52,998 52,998 52,998


0,024267 0,016833 0,020802 0,026237


99,788 101,52 100,15 96,947


90,835 90,721 92,406 87,471


77,746 81,665 81,169 73,724


172,07 172,07 172,07 172,07


78,335 78,335 78,335 78,335


67,437 77,051 71,399 67,437


45,663 46,794 46,143 45,663


772,73 807,96 787,68 772,73


57,115 46,034 52,082 57,115


2206 2206 2206 2206


0 0 0 0


0 0 0 0


0 0 0 0


274,4 274,4 274,4 274,4


224,69 224,69 224,69 224,69








B.14 PROPANE VESSEL

BLEVE - FIREBALL Case description: B.19 BLEVE FIRE BALL Model: BLEVE (Static model) version: 5.10 (22/11/2013) Reference: Yellow Book (CPR-14E), 3rd edition 1997, Paragraph 6.5.7 Parameters Inputs Chemical name (DIPPR) PROPANE (DIPPR) Total mass in vessel (kg) 15015 Initial temperature in vessel (°C) 19 Burst pressure vessel (bar) 25 Ambient temperature (°C) 19 Ambient relative humidity (%) 75 Amount of CO2 in atmosphere (%) 0,03 Distance from centre of vessel (Xd) (m) 1000 Exposure duration to heat radiation (s) 20 Take protective effects of clothing into account No X-coordinate of release (m) 0 Y-coordinate of release (m) 0 Calculate all contours for Physical effects Heat radiation level (lowest) for first contour plot (kW/m2) 7,3 Heat radiation level for second contour plot (kW/m2) 9,3 Heat radiation level (highest) for third contour plot (kW/m2) 13,4 Percentage of mortality for contour calculations (%)

Results Heat radiation at Xd (kW/m2) 1,0279 Heat radiation first contour at (m) 371,18 Heat radiation second contour at (m) 324,13 Heat radiation third contour at (m) 260,8 Heat emission from fire surface (kW/m2) 316,93 Duration of the fireball (s) 10,383 Radius of the Fire Ball (m) 73,776 Height bottom of the fire ball (m) 73,776 View factor (%) 0,53269 Atmospheric transmissivity (%) 60,885



Flame temperature (°C) 1264,9 Other information Main program Effects 8.1.8.6673 Chemical database DIPPR database Chemical source DIPPR Jan2010 Chemical source date 14/09/2010 Effects report created by ESLR2RH1F\andrea_silvasantos at 22/11/2013 13:27:34



DOMINO EFFECTS CALCULATIONS The calculation reports of the domino effect consequences for the proposed scenarios are shown below: B.01a – G1 Case description: B01a_TANK_G1_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D3 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01a_TANK_G1_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION D9 (linked to Pool evaporation - B01a_TANK_G1_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01a_TANK_G1_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION E5 (linked to Pool evaporation - B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) compared to: B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Parameters

Inputs

B01a_TANK_G1_D3_UVCE ED (linked to

Dense Gas Dispersion: Explosive mass -


Pool evaporation -B01a_TANK_G1_EVAP_D3 (linked to Liquefied Gas Bottom Discharge


ASE)))






ASE)))

B01a_TANK_G1_E5_UVCE ED (linked to


B01a_TANK_G1_DISPERSION E5 (linked to

Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge


ASE)))

B01b_TANK_G1_F2_UVCE ED (linked to


B01a_TANK_G1_DISPERSION F2 (linked to

Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge


ASE)))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


5155 0 2985,6 3,2752E05


8 8 8 8

Curve number

5 (Medium deflagration)5 (Medium deflagration) 5 (Medium deflagration) 5 (Medium deflagration)


50 50 50 50


107,49 0 105,22 992,22



point and cloud centre (m) Threshold overpressure (mbar)

160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results






ASE)))






ASE)))

B01a_TANK_G1_E5_UVCE ED (linked to


B01a_TANK_G1_DISPERSION E5 (linked to

Pool evaporation -B01a_TANK_G1_EVAP_E5 (linked to Liquefied Gas Bottom Discharge


ASE)))

B01b_TANK_G1_F2_UVCE ED (linked to


B01a_TANK_G1_DISPERSION F2 (linked to

Pool evaporation -B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge


ASE)))Confined mass in explosive range (kg)

412,4 0 238,85 26201


20633 -1E94 11950 1,3109E06


143,9 -1E98 119,14 206,07


20,924 -1E98 13,575 68,044




843,2 -1E100 587,9 5106,8


117,2 -1E103 98,69 495,65


44,805 -1E100 37,347 178,78













doors (7-15 kPa).






doors (7-15 kPa).





doors (7-15 kPa).









Moderate to minordamage. Deformed



















Large trees have fallen down (20-40

kPa). Walls made of concrete blocks have

collapsed (15-20). Minor damage to steel

frames (8-10 kPa). Connections between




failed 7-14 kPa). The roof of a storage tank has collapsed (7 kPa).





B.01b – G2 Case description: B01b_TANK_G1_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01a_TANK_G1_DISPERSION F2 (linked to Pool evaporation - B01a_TANK_G1_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01a_TANK_G1_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01b_TANK_G2_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D3 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION D9 (linked to Pool evaporation - B01b_TANK_G2_EVAP_D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION E5 (linked to Pool evaporation - B01b_TANK_G2_EVAP_E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) compared to: B01b_TANK_G2_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01b_TANK_G2_DISPERSION F2 (linked to Pool evaporation - B01b_TANK_G2_EVAP_F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01_b_TANK_G2_RELEASE))) Parameters

Inputs

B01b_TANK_G1_F2_UVCE ED

(linked to Dense Gas Dispersion:

Explosive mass -B01a_TANK_G1_D

ISPERSION F2 (linked to Pool evaporation -

B01a_TANK_G1_EVAP_F2 (linked to

Liquefied Gas Bottom Discharge

(TPDIS model) -B01a_TANK_G1_R

ELEASE)))

B01b_TANK_G2_D3_UVCE ED


Explosive mass -B01b_TANK_G2_D

ISPERSION D3 (linked to Pool evaporation -

B01b_TANK_G2_EVAP_D3 (linked to


(TPDIS model) -B01_b_TANK_G2_

RELEASE)))








RELEASE)))

B01b_TANK_G2_E5_UVCE ED



ISPERSION E5 (linked to Pool evaporation -

B01b_TANK_G2_EVAP_E5 (linked to



RELEASE)))





B01b_TANK_G2_EVAP_F2 (linked to



RELEASE)))Chemical name (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)

METHANE (DIPPR)


1,0151 1,0151 1,0151 1,0151 1,0151


3,2752E05 5250,3 698,1 2295,8 8,3549E05


8 8 8 8 8

Curve number






Distance from release

50 50 50 50 50



(Xd) (m) Offset between release point and cloud centre (m)

992,22 142,67 -9,2275 39,459 1130,1


160 160 160 160 160


0 0 0 0 0


0 0 0 0 0


N N N N N


0 0 0 0 0

Results



Explosive mass -B01a_TANK_G1_D


B01a_TANK_G1_EVAP_F2 (linked to


(TPDIS model) -B01a_TANK_G1_R

ELEASE)))








RELEASE)))








RELEASE)))

B01b_TANK_G2_E5_UVCE ED



ISPERSION E5 (linked to Pool evaporation -

B01b_TANK_G2_EVAP_E5 (linked to



RELEASE)))





B01b_TANK_G2_EVAP_F2 (linked to



RELEASE)))Confined mass in explosive range (kg)

26201 420,02 55,848 183,66 66839




1,3109E06 21014 2794,1 9188,8 3,344E06


206,07 144,77 74,014 109,28 206,07


68,044 21,174 4,3341 11,055 68,044


5106,8 853,35 229,21 495,99 6977,8


495,65 117,89 61,936 90,777 677,24


178,78 45,079 23,008 34,216 244,28


Pressure wave Pressure wave Pressure wave Pressure wave Pressure wave



kPa).


kPa).


kPa).


kPa).


kPa).



Partial roof failures, 25% of all brick

walls have failed,serious damage to

the remaining carrying elements.

Damage to windowframes and

doors (7-15 kPa).



walls have failed, serious damage to



doors (7-15 kPa).







walls have failed, serious damage to



doors (7-15 kPa).Damage to typical


walls and doors;





walls and doors;



American-style houses at Xd

failure of joints. Doors and window frames have failed. Wall covering has


storm; wooden walls fail,

breakage of windows (7-10

kPa).



kPa).



kPa).

failure of joints. Doors and window frames have failed. Wall covering has




displacement of foundation (20 kPa). Industrial

steel self-framing structure collapsed

(20-30 kPa). Cracking in empty

oil-storage tanks (20-30 kPa). Slight

deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down

(20-40 kPa). Walls made of concrete


steel frames (8-10 kPa). Connections




collapsed (7 kPa).

Minor damage to steel frames (8-10

kPa). Connections between steel or

aluminium ondulated plates have failed 7-14


collapsed (7 kPa).

Connections between steel or



collapsed (7 kPa).





collapsed (7 kPa).


displacement of foundation (20 kPa). Industrial

steel self-framing structure collapsed

(20-30 kPa). Cracking in empty

oil-storage tanks (20-30 kPa). Slight

deformation of a pipe-bridge (20-30 kPa). Large trees have fallen down

(20-40 kPa). Walls made of concrete


steel frames (8-10 kPa). Connections




collapsed (7 kPa). Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.01c – G3 Case description: B01c_TANK_G3_D3_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D3 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B01c_TANK_G3_D9_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION D9 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_E5_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION E5 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) compared to: B01c_TANK_G3_F2_UVCE ED (linked to Dense Gas Dispersion: Explosive mass - B01c_TANK_G3_DISPERSION F2 (linked to Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B01c_TANK_G3_RELEASE))) Parameters

Inputs

B01c_TANK_G3_D3_UVCE ED (linked to


B01c_TANK_G3_DISPERSION D3 (linked to

Pool evaporation - B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge

(TPDIS model) - B01c_TANK_G3_RELE

ASE)))




Pool evaporation -B01c_TANK_G3_EVAP_D3 (linked to Liquefied Gas Bottom Discharge

(TPDIS model) -B01c_TANK_G3_RELE

ASE)))

B01c_TANK_G3_E5_UVCE ED (linked to


B01c_TANK_G3_DISPERSION E5 (linked to



ASE)))

B01c_TANK_G3_F2_UVCE ED (linked to


B01c_TANK_G3_DISPERSION F2 (linked to



ASE)))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


2669,8 188,03 2389,4 5113,2


8 8 8 8

Curve number

5 (Medium deflagration) 5 (Medium deflagration)5 (Medium deflagration) 5 (Medium deflagration)


50 50 50 50


87,82 -9,0757 117,68 20,831

Threshold

160 160 160 160



overpressure (mbar) X-coordinate of release (m)

0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results






ASE)))






ASE)))

B01c_TANK_G3_E5_UVCE ED (linked to


B01c_TANK_G3_DISPERSION E5 (linked to



ASE)))

B01c_TANK_G3_F2_UVCE ED (linked to


B01c_TANK_G3_DISPERSION F2 (linked to



ASE)))Confined mass in explosive range (kg)

213,58 15,042 191,15 409,06


10686 752,59 9563,4 20466


114,71 48,506 110,69 143,49


12,474 1,4844 11,416 20,814


546,5 99,315 508,89 838,58

Positive phase

95,281 40,949 91,948 116,89



duration at Xd (ms) Dist. from center mass of cloud at threshold overpressure (m)

35,981 14,859 34,674 44,683













doors (7-15 kPa).







doors (7-15 kPa).





doors (7-15 kPa).Damage to typical American-style houses at Xd
























has collapsed (7 kPa). Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.02A – G1 Case description: HARDARM_L1_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L1_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L1_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION F2)) Parameters

Inputs

HARDARM_L1_L_UVCE D3 ED (linked to


HARDARM_L1_L_DISPERSION D3 (linked to

Pool evaporation -HARDARM_L1_L_EVA

PORATION D3))





PORATION D9))

HARDARM_L1_L_UVCE E5 ED (linked to


HARDARM_L1_L_DISPERSION E5 (linked to


PORATION E5))

HARDARM_L1_L_UVCE F2 ED (linked to


HARDARM_L1_L_DISPERSION F2 (linked to


PORATION F2))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


95750 35000 1,0534E05 53731


8 8 8 8

Curve number



100 100 100 100


239,77 162,39 130,23 535,58


160 160 160 160


0 0 0 0




0 0 0 0


N N N N


0 0 0 0

Results





PORATION D3))





PORATION D9))





PORATION E5))





PORATION F2))Confined mass in explosive range (kg)

7660 2800 8427,4 4298,5


3,8324E05 1,4009E05 4,2163E05 2,1506E05


186,89 135,85 191,52 156,71


39,917 18,348 42,915 25,521


2885,9 1511,4 3052,3 2001,1


308,84 222,52 318,75 255,38

Dist. from center mass of cloud at threshold

118,66 84,841 122,49 97,871



overpressure (m) Blast-wave shape at Xd












doors (7-15 kPa).





doors (7-15 kPa).





doors (7-15 kPa).





doors (7-15 kPa).





kPa).



windows (7-10 kPa).




kPa).




kPa).



(15-20). Minor damage to steel frames (8-10




collapsed (7 kPa).










collapsed (7 kPa).






collapsed (7 kPa). Other information Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.02B Case description: HARDARM_L2_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L2_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs





PORATION D3))





PORATION D9))





PORATION E5))








1,0151 1,0151 1,0151 1,0151


3067,5 242,34 1814,7 2837,5


8 8 8 8

Curve number



100 100 100 100


151,98 20,374 239,75 291,52


160 160 160 160


0 0 0 0




0 0 0 0


N N N N


0 0 0 0

Results





PORATION D3))





PORATION D9))





PORATION E5))






245,4 19,387 145,18 227


12278 969,98 7263,4 11357


60,772 25,904 51,851 59,221


2,631 1,0151 1,7118 2,4677


310,81 58,124 224,51 295,27


102,29 44,876 86,599 99,718


37,686 16,17 31,636 36,719


































B.03A Case description: B03a UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3 (linked to Pool evaporation - B03a EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03a UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D9 (linked to Pool evaporation - B03a EVAP D9)) compared to: B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5 (linked to Pool evaporation - B03a EVAP E5)) compared to: B03a UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP F2 (linked to Pool evaporation - B03a EVAP F2)) Parameters

Inputs

B03a UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3


EVAP D3))

B03a UVCE D9 ED (linked to Dense Gas Dispersion:

Explosive mass -B03a DISP D9 (linked to Pool

evaporation - B03a EVAP D9))

B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5


EVAP E5))

B03a UVCE F2 ED (linked to Dense Gas Dispersion:

Explosive mass -B03a DISP F2 (linked to Pool

evaporation - B03a EVAP F2))




1,0151 1,0151 1,0151 1,0151


24411 8985,2 27975 8896,7


8 8 8 8





50 50 50 50


100,19 93,352 47,564 515,01


160 160 160 160


0 0 0 0


0 0 0 0




270 270 270 270

Results

B03a UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP D3

(linked to Pool

B03a UVCE D9 ED (linked to Dense Gas Dispersion:

Explosive mass -B03a DISP D9

B03a UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03a DISP E5

(linked to Pool

B03a UVCE F2 ED (linked to Dense Gas Dispersion:

Explosive mass -B03a DISP F2



evaporation - B03a EVAP D3))


EVAP D9))




1952,9 718,82 2238 711,74


97704 35963 1,1197E05 35609


206,07 172,41 206,07 171,84


66,176 31,564 72,107 31,353


2138,5 1210,6 2277,9 1202,7


207,55 140,44 221,08 139,98


75,238 53,921 78,736 53,743






kPa).



kPa).




failed, serious damage to the remaining carrying

elements. Damage to windowframes and doors

(7-15 kPa).

Not habitable without major repair

works. Partial roof failures, 25% of all

brick walls have failed, serious damage to the

remaining carrying elements. Damage


kPa).



failed, serious damage to the remaining carrying

elements. Damage to windowframes and doors

(7-15 kPa).






kPa).


















framing structure collapsed (20-30 kPa).



10 kPa).


framing structure collapsed (20-30 kPa).



10 kPa).



Cracking in empty oil-storage tanks (20-30



blocks have collapsed (15-20). Minor damage








collapsed (7 kPa).

Cracking in empty oil-storage tanks (20-30



blocks have collapsed (15-20). Minor damage








collapsed (7 kPa).





B.03B Case description: B03b UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3 (linked to Pool evaporation - B03b EVAP D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B03b UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D9 (linked to Pool evaporation - B03b EVAP D9)) compared to: B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5 (linked to Pool evaporation - B03b EVAP E5)) compared to: B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2 (linked to Pool evaporation - B03b EVAP F2)) Parameters

Inputs

B03b UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP D3


EVAP D3))



EVAP D9))

B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5


EVAP E5))

B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2





1,0151 1,0151 1,0151 1,0151


152,77 179,75 151,83 0


8 8 8 8


deflagration)5 (Medium




50 50 50 50


19,989 17,728 24,312 -1,5E100


160 160 160 160


0 0 0 0


0 0 0 0




270 270 270 270

Results



EVAP D3))



EVAP D9))

B03b UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP E5


EVAP E5))

B03b UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B03b DISP F2



12,222 14,38 12,147 0

Total 611,48 719,46 607,7 -1E94



combustion energy (MJ) Peak overpressure at Xd (mbar)

44,536 47,613 44,432 -1E98


1,2367 1,4296 1,2296 -1E98


85,25 96,169 84,877 -1E100


38,284 40,396 38,206 -1E103


13,865 14,638 13,837 -1E100




























B04A Case description: HARDARM_L1_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L1_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION D9)) compared to: HARDARM_L1_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L1_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L1_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs HARDARM_L1_L_UVC

E D3 ED (linked to Dense Gas Dispersion:


Dense Gas Dispersion:







Explosive mass -HARDARM_L1_L_DISP

ERSION D3 (linked to Pool evaporation -

HARDARM_L1_L_EVAPORATION D3))


ERSION D9 (linked to Pool evaporation -

HARDARM_L1_L_EVAPORATION D9))


ERSION E5 (linked to Pool evaporation -

HARDARM_L1_L_EVAPORATION E5))


ERSION F2 (linked to Pool evaporation -

HARDARM_L2_L_EVAPORATION F2))




1,0151 1,0151 1,0151 1,0151


1,1043E05 20467 27525 2837,5


8 8 8 8

Curve number



100 100 100 100


262,44 162,78 949,54 291,52


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0



Results





PORATION D3))





PORATION D9))





PORATION E5))






8834,6 1637,3 2202 227


4,4201E05 81918 1,1017E05 11357


193,85 113,15 125 59,221


44,49 12,063 15,101 2,4677


3138,1 1063,5 1289,8 295,27


323,77 187,97 206,36 99,718


124,44 70,946 78,311 36,719





















doors (7-15 kPa).



doors (7-15 kPa).



doors (7-15 kPa).





kPa).



windows (7-10 kPa).



windows (7-10 kPa).








collapsed (7 kPa).














B04B Case description: HARDARM_L2_L_UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D3 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D3)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: HARDARM_L2_L_UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION D9 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION D9)) compared to: HARDARM_L2_L_UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION E5 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION E5)) compared to: HARDARM_L2_L_UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - HARDARM_L2_L_DISPERSION F2 (linked to Pool evaporation - HARDARM_L2_L_EVAPORATION F2)) Parameters

Inputs





PORATION D3))





PORATION D9))





PORATION E5))








1,0151 1,0151 1,0151 1,0151


3067,5 242,34 1814,7 2837,5


8 8 8 8

Curve number



100 100 100 100


151,98 20,374 239,75 291,52


160 160 160 160


0 0 0 0




0 0 0 0


N N N N


0 0 0 0

Results





PORATION D3))





PORATION D9))





PORATION E5))






245,4 19,387 145,18 227


12278 969,98 7263,4 11357


60,772 25,904 51,851 59,221


2,631 1,0151 1,7118 2,4677


310,81 58,124 224,51 295,27


102,29 44,876 86,599 99,718


37,686 16,17 31,636 36,719


































B.05.REV Case description: tank (secondary pump) to compressor - uvce D3 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D3 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D3 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: tank (secondary pump) to compressor - uvce D9 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion D9 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation D9 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce E5 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion E5 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation E5 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) compared to: tank (secondary pump) to compressor - uvce F2 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to compressor - dispersion F2 PNEW (linked to Pool evaporation - onboard tank (secondary pump) to compressor - evaporation F2 PNEW (linked to Liquefied Gas Bottom Discharge (TPDIS model) - onboard tank to compressor - release PNEW))) Parameters

Inputs

tank (secondary pump) to compressor - uvce

D3 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to

compressor -dispersion D3 PNEW

(linked to Pool evaporation - onboard


evaporation D3 PNEW (linked to Liquefied

Gas Bottom Discharge (TPDIS model) -onboard tank to

compressor - release PNEW)))


D9 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank(secondary pump) to








E5 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to

compressor -dispersion E5 PNEW



evaporation E5 PNEW (linked to Liquefied




F2 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to

compressor -dispersion F2 PNEW



evaporation F2 PNEW (linked to Liquefied






1,0151 1,0151 1,0151 1,0151


22341 17878 18047 66077


8 8 8 8

Curve number






50 50 50 50




429,91 -9,8282 33,214 33,547


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results


















E5 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to

compressor -dispersion E5 PNEW



evaporation E5 PNEW (linked to Liquefied




F2 LC1 PNEW ED (linked to Dense Gas Dispersion: Explosive mass - onboard tank (secondary pump) to

compressor -dispersion F2 PNEW



evaporation F2 PNEW (linked to Liquefied




1787,3 1430,2 1443,8 5286,1


89419 71556 72233 2,6447E05


206,07 201,73 201,99 206,07


62,038 53,59 53,914 92,932


2052,5 1812,2 1822,4 3385,4


199,21 179,67 180,45 328,57

Dist. from center mass of cloud at

73,049 67,819 68,032 104,86



threshold overpressure (m) Blast-wave shape at Xd












doors (7-15 kPa).





doors (7-15 kPa).





doors (7-15 kPa).

Not habitable withoutmajor repair works. Partial roof failures,




doors (7-15 kPa).





kPa).




kPa).




kPa).




kPa).




framing structure collapsed (20-30 kPa). Cracking in empty oil-storage tanks (20-30

kPa). Slight deformation of a pipe-

bridge (20-30 kPa). Large trees have fallen

down (20-40 kPa). Walls made of

concrete blocks have collapsed (15-20).









































B.06.REV Case description: B06_onboard tank (secondary pump) to compressor - UVCE D3 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D3 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B06_onboard tank (secondary pump) to compressor - UVCE D9 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion D9 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06_onboard tank (secondary pump) to compressor - UVCE E5 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion E5 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) compared to: B06_onboard tank (secondary pump) to compressor - UVCE F2 ED (linked to Dense Gas Dispersion: Explosive mass - B06_onboard tank (secondary pump) to compressor - dispersion F2 (linked to Pool evaporation - B06_onboard tank (secondary pump) to compressor - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B06.rev_onboard tank to compressor - release))) Parameters

Inputs

B06_onboard tank (secondary pump) to compressor - UVCE

D3 ED (linked to Dense Gas

Dispersion: Explosive mass - B06_onboard


dispersion D3 (linked to Pool evaporation -

B06_onboard tank (secondary pump) to



(TPDIS model) -B06.rev_onboard tank

to compressor -release)))












E5 ED (linked to Dense Gas



dispersion E5 (linked to Pool evaporation -







F2 ED (linked to Dense Gas



dispersion F2 (linked to Pool evaporation -









1,0151 1,0151 1,0151 1,0151


1275,3 0 397,55 3675,8


8 8 8 8

Curve number






50 50 50 50

Offset between

118,94 0 0 161,08



release point and cloud centre (m) Threshold overpressure (mbar)

160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0

Results






















E5 ED (linked to Dense Gas



dispersion E5 (linked to Pool evaporation -







F2 ED (linked to Dense Gas



dispersion F2 (linked to Pool evaporation -







102,03 0 31,804 294,07


5104,4 -1E94 1591,2 14713


90,116 -1E98 61,505 127,83


6,9186 -1E98 2,714 15,857


338,56 -1E100 159,14 673,34


75,139 -1E103 51,75 105,34

Dist. from 28,127 -1E100 19,071 40,028



center mass of cloud at threshold overpressure (m) Blast-wave shape at Xd

















doors (7-15 kPa).




windows (7-10 kPa).





windows (7-10 kPa).















B.07 Case description: B07_pump to ru - uvce D3 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D3 (linked to Pool evaporation - B07_pump to RU - evaporation D3 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B07_pump to ru - uvce D9 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion D9 (linked to Pool evaporation - B07_pump to RU - evaporation D9 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce E5 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion E5 (linked to Pool evaporation - B07_pump to RU - evaporation E5 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) compared to: B07_pump to ru - uvce F2 ED (linked to Dense Gas Dispersion: Explosive mass - B07_pump to ru - dispersion F2 (linked to Pool evaporation - B07_pump to RU - evaporation F2 (linked to Liquefied Gas Bottom Discharge (TPDIS model) - B07_pump to ru - release))) Parameters

Inputs

B07_pump to ru -uvce D3 ED (linked to

Dense Gas Dispersion: Explosive mass - B07_pump to

ru - dispersion D3 (linked to Pool evaporation -

B07_pump to RU -evaporation D3

(linked to Liquefied Gas Bottom

Discharge (TPDIS model) - B07_pump

to ru - release)))


Dense GasDispersion: Explosive mass - B07_pump to





to ru - release)))

B07_pump to ru - uvce E5 ED (linked to


ru - dispersion E5 (linked to Pool evaporation -




release)))

B07_pump to ru - uvce F2 ED (linked to Dense

Gas Dispersion: Explosive mass -B07_pump to ru -

dispersion F2 (linked to Pool evaporation -B07_pump to RU -



ru - release)))




1,0151 1,0151 1,0151 1,0151


1834,7 190,3 669,32 4050,5


8 8 8 8






50 50 50 50


78,783 -8,1074 44,423 113,01


160 160 160 160


0 0 0 0


0 0 0 0


N N N N




0 0 0 0

Results







to ru - release)))







to ru - release)))

B07_pump to ru - uvce E5 ED (linked to


ru - dispersion E5 (linked to Pool evaporation -




release)))

B07_pump to ru - uvce F2 ED (linked to Dense

Gas Dispersion: Explosive mass -B07_pump to ru -

dispersion F2 (linked to Pool evaporation -B07_pump to RU -



ru - release)))


146,77 15,224 53,546 324,04


7343,2 761,68 2679 16212


101,67 48,747 73,026 132,22


9,2877 1,4994 4,1851 17,037


429,45 100,16 223,17 717,99


84,475 41,096 61,121 108,6


31,752 14,919 22,688 41,344



















doors (7-15 kPa).Damage to Minor damage. No damage or very Minor damage. Minor damage.



typical American-style houses at Xd

Comparable to a damage due to a


windows (7-10 kPa).

minor damage Comparable to a damage due to a


windows (7-10 kPa).

Comparable to a damage due to a storm;

wooden walls fail, breakage of windows (7-

10 kPa).


Minor damage to steel frames (8-10 kPa). Connections

between steel or aluminium ondulated plates have failed 7-

14 kPa). The roof of a storage tank has

collapsed (7 kPa).



aluminium ondulated plates have failed 7-

14 kPa). The roof of a storage tank has

collapsed (7 kPa).









B.08.REV Case description: B08_rev_vaporizer - uvce D3 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D3 pnew)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B08_rev_vaporizer - uvce D9 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE D9 pnew)) compared to: B08_rev_vaporizer - uvce E5 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE E5 pnew)) compared to: B08_rev_vaporizer - uvce F2 pNew ED (linked to Neutral Gas Dispersion: Explosive mass - B08_rev_vaporizer - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B08_rev_vaporizer - JFIRE F2 pnew)) Parameters

Inputs

B08_rev_vaporizer -uvce D3 pNew ED

(linked to Neutral Gas Dispersion: Explosive

mass -B08_rev_vaporizer -dispersion D3 pNew

(linked to Gas Jet Fire (Chamberlain model) -

B08_rev_vaporizer -JFIRE D3 pnew))






B08_rev_vaporizer -uvce E5 pNew ED


mass -B08_rev_vaporizer -dispersion E5 pNew


B08_rev_vaporizer -JFIRE E5 pnew))

B08_rev_vaporizer -uvce F2 pNew ED


mass -B08_rev_vaporizer -dispersion F2 pNew


B08_rev_vaporizer -JFIRE F2 pnew))




1,0151 1,0151 1,0151 1,0151


294,14 49,962 199,8 853,01


8 8 8 8

Curve number






50 50 100 100


61,03 31,015 69,31 213,66


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0



(deg)

Results











B08_rev_vaporizer -uvce E5 pNew ED


mass -B08_rev_vaporizer -dispersion E5 pNew


B08_rev_vaporizer -JFIRE E5 pnew))

B08_rev_vaporizer -uvce F2 pNew ED


mass -B08_rev_vaporizer -dispersion F2 pNew


B08_rev_vaporizer -JFIRE F2 pnew))


23,531 3,997 15,984 68,241


1177,3 199,97 799,7 3414,1


55,687 30,152 24,38 38,871


2,1376 1,0151 1,0151 1,0151


130,6 39,904 51,326 132,15


46,905 26,469 42,105 67,994


17,249 9,5527 15,163 24,598


Pressure wave Shock Wave Shock Wave Pressure wave


























Other information



Main program Effects 8.1.8.6673Chemical database DIPPR databaseChemical source DIPPR Jan2010Chemical source date 14/09/2010




B.09.REV Case description: B09_RU to ME - UVCE D3 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D3 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D3 pNew)) Model: Explosion (Multi Energy model) version: 5.03 (15/11/2013) Reference: Yellow Book CPR14E 3rd Edition - Chapter 5: Vapour cloud explosions compared to: B09_RU to ME - UVCE D9 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion D9 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE D9 pNew)) compared to: B09_RU to ME - UVCE E5 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE E5 pNew)) compared to: B09_RU to ME - UVCE F2 ED (linked to Neutral Gas Dispersion: Explosive mass - B09_RU to ME - dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain model) - B09_RU to ME - JFIRE F2 pNew)) Parameters

Inputs

B09_RU to ME - UVCE D3 ED (linked to Neutral Gas

Dispersion: Explosive mass - B09_RU to ME -

dispersion D3 pNew (linked to Gas Jet Fire

(Chamberlain model) -B09_RU to ME - JFIRE D3

pNew))

B09_RU to ME -UVCE D9 ED (linked

to Neutral Gas Dispersion: Explosive

mass - B09_RU to ME - dispersion D9

pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE D9

pNew))

B09_RU to ME -UVCE E5 ED (linked



dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE E5

pNew))

B09_RU to ME -UVCE F2 ED (linked



dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE F2

pNew))Chemical name (DIPPR)



1,0151 1,0151 1,0151 1,0151


25245 10173 22558 24903


8 8 8 8





50 50 100 100


399,32 235,45 529,18 466,3


160 160 160 160


0 0 0 0


0 0 0 0


N N N N


0 0 0 0



(deg)

Results

B09_RU to ME - UVCE D3 ED (linked to Neutral Gas

Dispersion: Explosive mass - B09_RU to ME -

dispersion D3 pNew (linked to Gas Jet Fire

(Chamberlain model) -B09_RU to ME - JFIRE D3

pNew))

B09_RU to ME -UVCE D9 ED (linked

to Neutral Gas Dispersion: Explosive

mass - B09_RU to ME - dispersion D9

pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE D9

pNew))

B09_RU to ME -UVCE E5 ED (linked



dispersion E5 pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE E5

pNew))

B09_RU to ME -UVCE F2 ED (linked



dispersion F2 pNew (linked to Gas Jet Fire (Chamberlain

model) - B09_RU to ME - JFIRE F2

pNew))Confined mass in explosive range (kg)

2019,6 813,87 1804,6 1992,3


1,0104E05 40719 90286 99675


206,07 179,26 116,86 120,84


67,816 35,059 13 14,011


2172 1311,6 1132,7 1208,3


210,81 146,33 193,87 199,98


76,086 56,2 73,284 75,741






kPa).


kPa).


kPa).




carrying elements. Damage to windowframes and doors

(7-15 kPa).





doors (7-15 kPa).






kPa).






kPa).Damage to typical American-style houses at Xd


and doors; failure of joints. Doors and window frames have failed. Wall covering



and window frames


storm; wooden walls fail, breakage


storm; wooden walls fail, breakage



has fallen down (15 kPa). have failed. Wall covering has fallen

down (15 kPa).

of windows (7-10 kPa).

of windows (7-10 kPa).




kPa). Cracking in empty oil-storage tanks (20-30 kPa).

Slight deformation of a pipe-bridge (20-30 kPa).











collapsed (7 kPa).





collapsed (7 kPa).





collapsed (7 kPa).





B.10 NO EXPLOSIVE MASS B.11 NO EXPLOSIVE MASS B.12 NO EXPLOSIVE MASS B.13 NO EXPLOSIVE MASS

CONSEQUENCE CALCULATIONS - Environment and … DPS_QRA Annex E... · CONSEQUENCE CALCULATIONS B.01a - GAS TANKER (RELEASE ON WATER) RELEASE Case description: B01a_TANK_G1_RELEASE

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