BMB Jaber Hospital Plumbing Pumps Calculations CALCULATION SHEET Project Name: JABER HOSPITAL Date: Job No. Main Hospital Building 27/07/2011 090512 Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no: Cooling Tower Make Up Pump HPS-01 Sizing SJN Reference Calculations Output Cooling Tower Make-Up Pump HPS-1 Location: Basement (-9.53 level) Application: To pump water from HVAC Make UpTank(-9.53 level) to Cooling Tower at -2.0 level Pumps set : 3 pumps in one set, Three working ,each pump capacit 40 m3/hr(1 Set is working 1 Set standby) - Static Head = 23 m - Residual Pressu = 10 m ρ = 990 Kg/m³ @45° C - Friction Losses:- ɡ = 9.8 C = 150 For pipes Nodes Flow Rate (gpm) Velocity-V(m/sec) Fittings* Friction Losses(pa/mtr) Friction Losses in Pipe (Kp 1 - 2 150 174 529 1.88 11 E-90 53.57 270.54 182.23 49.30 2 TEE 18.28 3 G.V 6.39 0 E-45 0 1 C.V 18.3 49.30 * -The mentioned fitting are the fittings on this pipe segment. - G.V: Gate Valve, E-90: ninety degree Elbow. ** -LE : Equivelent Length for each fitting. - Total Length= LE+ Pipe Distance. - Total Friction Losses in pipes and = 49.30 Kpa = 0.49 Bar = 4.93 m '- Total Pump Head require = 23 + 10 + 4.93 = 37.93 m = 3.79 Bar = 37.93 M Say 38 mtr Selected pump 40 m3/hr @ 50 mtr head is sufficient Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C) 1.852 x (1 / D) 1.167 x (r g) m/sec 2 Pipe Size- D(mm) Distance- L (m) LE/ fitting** Total Length***
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Main Hospital Building 27/07/2011 090512Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no:
Cooling Tower Make Up Pump HPS-01 Sizing SJNReference Calculations Output
Cooling Tower Make-Up Pump HPS-1Location: Basement (-9.53 level)Application: To pump water from HVAC Make UpTank(-9.53 level) to Cooling Tower at -2.0 level Pumps set : 3 pumps in one set, Three working ,each pump capacity is 40 m3/hr(1 Set is working 1 Set standby)- Static Head = 23 m- Residual Pressure = 10 m
ρ = 990 Kg/m³ @45° C
- Friction Losses:- ɡ = 9.8C = 150 For pipes
Nodes Distance- L (m) Flow Rate (gpm) Velocity-V(m/sec) Fittings* LE/fitting** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
1 - 2 150 174 529 1.88
11 E-90 53.57
270.54 182.23 49.30
2 TEE 18.283 G.V 6.390 E-45 01 C.V 18.3
49.30
* -The mentioned fitting are the fittings on this pipe segment.- G.V: Gate Valve, E-90: ninety degree Elbow.
** -LE : Equivelent Length for each fitting.- Total Length= LE+ Pipe Distance.
- Total Friction Losses in pipes and fittings = 49.30 Kpa = 0.49 Bar = 4.93 m'- Total Pump Head required = 23 + 10 + 4.93
= 37.93 m = 3.79 Bar= 37.93 M Say 38 mtr
Selected pump 40 m3/hr @ 50 mtr head is sufficient
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
Main Hospital Building 27/07/2011 090512Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no:
Transfer Pump TR-1 Sizing SJNReference Calculations Output
Transfer Pump TR-1Location: Basement (-9.53 level)Application: To pump water from Break Water tank(-9.53 level) to Potable & Fire Water Tank(-9.53 level)
Pumps set :- Static Head = 7 m- Residual Pressure = 10 m
ρ = 990 Kg/m³ @45° C
- Friction Losses:- ɡ = 9.8C = 150 For pipes
Nodes Distance- L (m) Flow Rate (gpm) Velocity-V(m/sec) Fittings* LE/fitting** Total Length*** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
1 - 2 150 61 397 1.41
3 E-90 18.3
109.6 107.09 11.741 TEE 9.21 G.V 2.11 C.V 19
11.74
* -The mentioned fitting are the fittings on this pipe segment.- G.V: Gate Valve, E-90: ninety degree Elbow.
** -LE : Equivelent Length for each fitting.- Total Length= LE+ Pipe Distance.Pressure drop in Sand filter = 7psi = 5 mtr
- Total Friction Losses in pipes and fittings = 11.74 Kpa = 0.12 Bar = 1.17 m'- Total Pump Head required = 7 + 10 + 1.17 + 5
= 23.17 m = 2.32 Bar= 23.17 Say 23.5 mtr=
Selected pump is 30m3/hr @ 25 mtr head is sufficient
4 pumps, Three working and one standby,each pump capacity is 30 m3/hr
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
Booster Pump BP-3Location: Basement at -9.53 Level Water Tank BuildingApplication: To pump water from basement to Residential building Pumps set : 3 pumps in one set are working each pump capacity is 20 m3/hr '@ 65 Mtr Head(1 Set is working 1 Set standby)- Static Head = 22.50 m- Residual Pressure = 10 hose bib at highest level(+12.2mtr)
water closet comes +8.7 level onwards to down, where avilable pressure is 19.5 psi, which is more than enough to operate the fliush valve of W.C
Total flow of three pumps = 60 m3/hr
= 264 gpm ρ = 1000 Kg/m³
ɡ = 9.8 C = 150 For copper pipes
Nodes Pipe Size(mm) Distance- L (m) Flow Rate (gpm) Velocity(m/sec) Fittings* LE/fitting** Total Length*** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
A -B 102.2 6.4 132 1.01
E-90 0
7.77 91.23 0.71TEE 0
1 G.V 1.37C.V 0
B-C 130.8 11.5 132 0.62
E-90 0
20.6 27.43 0.571 TEE 9.1
G.VC.V
C-D 130.8 19.5 264 1.23
E-90 0
39.8 99.02 3.942 TEE 18.21 G.V 2.1
C.V
D-E 130.8 1 176 0.82
E-90 0
10.1 46.73 0.471 TEE 9.1
G.VC.V
E-F 130.8 1 88 0.41
E-90 0
19.2 12.94 0.252 TEE 18.2
G.VC.V
F-G 102.2 2 88 0.67
E-90 0
16.93 43.06 0.73TEE 0
2 G.V 2.741 C.V 12.19
G-H 130.8 1 88 0.41
E-90 0
19.2 12.94 0.252 TEE 18.2
G.VC.V
H-I 130.8 1 176 0.82
E-90 0
10.1 46.73 0.471 TEE 9.1
G.VC.V
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
- Total Friction Losses in pipes and fittings = 258.79 kpa = 25.88 mtr
Pressure drop in catridge filter = 2.54 mtr
Static Head = 22.50 mtr
Residual pressure = 10 mtr
Head avilable in the suction side due to to the height of water coumn in the tank = 3.5 mtr Catridge Filter SS-12 - three set being used for filteration
12 catridges in two layers inside the housing
Pressure drop (attached document) =0.042psi/gpm
- Total Pump Head required = 57.42 mtr Presure drop for 88 Gpm (one third of the total flow-264 gpm) =3.69psi= 2.54 mtr
Selected pump of 20m3/hr @ 65 mtr head is sufficient
Booster Pump BP-3Location: Basement at -9.53 Level Water Tank BuildingApplication: To pump water from basement to Residential building Pumps set : 3 pumps in one set are working each pump capacity is 20 m3/hr '@ 65 Mtr Head(1 Set is working 1 Set standby)- Static Head = 22.50 m- Residual Pressure = 10 m
ρ = 1000 Kg/m³- Friction Losses:- ɡ = 9.8
C = 150 For copper pipes
Nodes Pipe Size(mm) Distance- L (m) Flow Rate (gpm) Velocity(m/sec) Fittings* LE/fitting** Total Length*** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
A -B 100 4 132 1.06
E-90 0
5.37 101.44 0.54TEE 0
1 G.V 1.37C.V 0
B-C 150 11.5 132 0.47
E-90 0
20.6 14.08 0.291 TEE 9.1
G.VC.V
C-D 150 19.5 264 0.94
E-90 0
39.8 50.81 2.022 TEE 18.21 G.V 2.1
C.V
D-E 150 1 176 0.63
E-90 0
10.1 23.98 0.241 TEE 9.1
G.VC.V
E-F 150 1 88 0.31
E-90 0
19.2 6.64 0.132 TEE 18.2
G.VC.V
F-G 100 2 88 0.70
E-90 0
16.93 47.87 0.81TEE 0
2 G.V 2.741 C.V 12.19
G-H 150 1 88 0.31
E-90 0
19.2 6.64 0.132 TEE 18.2
G.VC.V
H-I 150 1 176 0.63
E-90 0
10.1 23.98 0.241 TEE 9.1
G.VC.V
I-J 150 2 264 0.94
1 E-90 6.1
28.4 50.81 1.442 TEE 18.21 G.V 2.1
C.V
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
Main Hospital Building 17/9/2011 090512Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no:
Booster Pump BP-4 TO BP-8 Sizing SJNReference Calculations Output
Booster Pump BP-4 TO BP-8 (TYPICAL)Location: Basement Application: To pump water from Tower 60 Level to 35 LevelPumps set : 2 pumps in one set are working ,each pump capacity is 29 m3/hr '@35 mtr Head(1 Set is working 1 Set standby)- Static Head = 5 m- Residual Pressure = 10 m
ρ = 1000 Kg/m³- Friction Losses:- ɡ = 9.8
C = 150 For pipes
Nodes Pipe Size(mm) Velocity(m/sec) Fittings* LE/fitting** Total Length*** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
1 - 2 100 1.5 256 2.05
E-90
21.47 345.90 7.431 TEE 6.4
1 G.V 1.381 C.V 12.19
2 -3 100 19 256 2.05
3 E-90 9.12
35.9 345.90 12.421 TEE 6.41 G.V 1.38
C.V
3 -4 25 2 5 0.64
E-90
4.52 202.31 0.911 TEE 1.521 G.V 1
C.V
4 - 5 20 6.5 4 0.80
E-90 0
7.71 396.82 3.061 TEE 1.21
G.V 0C.V
5 - 6 15 25 3 1.07
3 E-90 1.44
26.71 945.76 25.26TEE 0
1 G.V 0.27C.V
49.08
* -The mentioned fitting are the fittings on this pipe segment.- G.V: Gate Valve, E-90: ninety degree Elbow.
** -LE : Equivelent Length for each fitting.- Total Length= LE+ Pipe Distance.
Pressure drop in catridge filter = 7psi = 5 mtr- Total Friction Losses in pipes and fittings = 49.08 Kpa = 0.49 Bar = 4.91 m
'- Total Pump Head required = 5 + 10 + 4.91 + 5= 24.91 m = 2.49 Bar
Selected pump of 29m3/hr @ 35 mtr head is sufficient
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
m/sec2
Distance- L (m)
Flow Rate (gpm)
C17
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BMBJaber Hospital
PlumbingPumps Calculations
CALCULATION SHEET
Project Name: JABER HOSPITAL Date: Job No.
Shelter Building 8/8/2011 05020
Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no:
Booster Pump BP-1 & 2 Sizing SJN
Reference Calculations Output
Booster Pump BP-1 & BP-2Location: Basement Application: To pump water from basement to Shelter Area at -5.0 LevelPumps set : 2 pumps in one set each pump capacity is 17 m3/hr @45 mtr Head(One Working One Standby)- Static Head = 4.00 m- Residual Pressure = 15 m
ρ = 990 Kg/m@45° C
- Friction Losses:- ɡ = 9.8C = 150 For pipes
Nodes Pipe Size(mm) Distance- L (m) Flow Rate (gpm) Velocity(m/sec) Fittings* LE/fitting** Total Length*** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
1 -2 65 15 75 1.42
3 E-90 5.46
32.58 287.37 9.361 TEE 3.651 G.V 0.851 C.V 7.62
2 - 3 65 1 75 1.42
E-90
4.65 287.37 1.341 TEE 3.65
G.VC.V
3 -4 65 8.5 44 0.83
E-90 0
12.15 107.03 1.301 TEE 3.65
G.V 0C.V
4- 5 65 19.5 43 0.81
1 E-90 1.82
24.97 102.57 2.561 TEE 3.65
G.V 0C.V
5- 6 25 11.5 5 0.64
1 E-90 0.8
14.82 200.29 2.971 TEE 1.521 G.V 1
C.V
6- 7 25 3.6 4 0.51
2 E-90 1.6
6.2 132.49 0.82TEE 0
1 G.V 1C.V
18.35
* -The mentioned fitting are the fittings on this pipe segment.- G.V: Gate Valve, E-90: ninety degree Elbow.
** -LE : Equivelent Length for each fitting.- Total Length= LE+ Pipe Distance.Pressure drop in catridge filter = 7psi = 5 mtr
- Total Friction Losses in pipes and fittings = 18.35 Kpa = 0.18 Bar = 1.83 m
m/sec2
C19
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BMBJaber Hospital
PlumbingPumps Calculations
'- Total Pump Head required = 4.00 + 15 + 1.83 + 5= 25.83 m = 2.58 Bar
Selected pump of 17m3/hr @ 45 mtr head is sufficient
Liftingr PumpLPS-02Location: Basement (-9.53 level)Application: To pump water from Potable Water tank(-9.53 level) to GRP water Tank at Tower C,D& E(+60.0level)
Pumps set :- Static Head = 73 m- Residual Pressure = 10 m
ρ = 990 Kg/m³ @45° C
- Friction Losses:- ɡ = 9.8C = 150 For pipes
Nodes Distance- L (m) Flow Rate (gpm) Velocity-V(m/sec) Fittings* LE/fitting** Friction Losses(pa/mtr) Friction Losses in Pipe (Kpa)
1 - 2 100 754 225 1.80
30 E-90 91.44
868.41 306.38 266.06
1 TEE 6.44 G.V 1.372 E-45 3.21 C.V 12
266.06
* -The mentioned fitting are the fittings on this pipe segment.- G.V: Gate Valve, E-90: ninety degree Elbow.
** -LE : Equivelent Length for each fitting.- Total Length= LE+ Pipe Distance.Pressure drop in catridge filter = 7psi = 5 mtr
- Total Friction Losses in pipes and fittings = 266.06 Kpa = 2.66 Bar = 26.61 m'- Total Pump Head required = 73 + 10 + 26.61 = 5
= 114.61 m = 11.46 Bar= 114.61 Say 112 mtr=
Selected pump is 17m3/hr @ 113 mtr head is sufficient
3 pumps in one set, Three working ,each pump capacity is 22 m3/hr(1 Set is working 1 Set standby)
Pressure drop in straight pipe (Pa) = 6.819 x L x (V / C)1.852 x (1 / D)1.167 x ( r g)
m/sec2
Pipe Size-D(mm)
Total Length***
C26
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BMBJaber Hospital
PlumbingPumps Calculations
CALCULATION SHEET
Project Name: JABER HOSPITAL Date: Job No.
Main Hospital Building 4/9/2011 090512
Calculation Title: WATER SUPPLY SYSTEM Engineer: Sheet no: