8/3/2019 LIS-OO-0003-0
1/31
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC)
(EIL)
NATIONAL IRANIAN OIL ENGINEERING &
CONSTRUCTION COMPANY (NIOEC)
BANDAR ABBASGAS CONDENSATE REFINERY
PROJECT
NIOEC Job No.: 226210
Unit No.: 02 Unit: NHTDoc Title: LINE LIST
OD&CC Job No.: RF-01
Doc No.: 02/EB-PR/LIS-OO-0003-0 Rev : 0 Page 1 of 35
0
LINE LIST
8/3/2019 LIS-OO-0003-0
2/31
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC)
(EIL)
NATIONAL IRANIAN OIL ENGINEERING &
CONSTRUCTION COMPANY (NIOEC)
BANDAR ABBASGAS CONDENSATE REFINERY
PROJECT
NIOEC Job No.: 226210
Unit No.: 02 Unit: NHTDoc Title: LINE LIST
OD&CC Job No.: RF-01
Doc No.: 02/EB-PR/LIS-OO-0003-0 Rev : 0 Page 2 of 35
Revision Index
Sheet No.Revision
Sheet No.Revision
0 1 2 3 4 0 1 2 3 41 X
2 X
3 X
4 X
5 X
6 X
7 X
8 X
9 X
10 X
11 X
12 X
13 X
14 X
15 X
16 X
8/3/2019 LIS-OO-0003-0
3/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 5 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 01/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/3
8/3/2019 LIS-OO-0003-0
4/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0101-A1A3F-12"- BL FV-02-003 HC 6.0 40 L 373 880 703.3 0.34 8.0 85 40 0.68 2.05
PRO-02-0102-A1A3F-12"- FV-02-003 VH-0201 HC 2.5 40 L 373 843 702.7 0.34 4.5 85 40 1.66 2.05
PRO-02-0103-A1A3F-14"- VH-0201 PRO-1004 HC 2.5 40 L 373 843 702.7 0.34 5.1 85 40 0.42 1.69
PRO-02-0104-A1A3F-12"- PRO-0103 P-0201 A HC 2.5 40 L 186 922 702.7 0.34 5.1 85 40 1.66 1.02
PRO-02-0105-A1A3F-12"- PRO-0103 P-0201 B HC 2.5 40 L 186 922 702.7 0.34 5.1 85 40 0.68 1.02
PRO-02-0106-A1A3F-12"- PRO-0103 P-0201 C HC 2.5 40 L 186 922 702.7 0.34 5.0 85 40 0.18 1.02
PRO-02-0107-A3A3F-8"- P-0201 A PRO-0110 HC 36.4 40 L 186 922 707.7 0.35 46.9(1)
85 40 1.36 2.27 (1) (1) P-0201 A/B shut off pressure
PRO-02-0108-A3A3F-8"- P-0201 B PRO-0107 HC 36.4 40 L 186 922 707.7 0.35 46.9(1)
85 40 1.36 2.27 (1) (1) P-0201 A/B shut off pressure
PRO-02-0109-A3A3F-8"- P-0201 C PRO-0107 HC 36.4 40 L 186 922 707.7 0.35 46.9(1)
85 (207) 1.22 2.18 (1) (1) P-0201 A/B shut off pressure
PRO-02-0110-A3A3F-12"- PRO-0107 FV-02-002 HC 36.4 40 L 373 843 707.7 0.35 46.9(1)
85 40 0.68 2.03 (1) (1) P-0201 A/B shut off pressure
PRO-02-0111-A3A3F-12"- FV-02-002 F-0201 A HC 30.1 40 L 373 843 706.1 0.35 46.9(1)
85 40 0.68 2.04 (1) (1) P-0201 A/B shut off pressure
PRO-02-0112-A3A3F-12"- PRO-0111 F-0201 B HC 30.1 40 L 373 843 706.1 0.35 46.9(1)
85 40 0.68 2.04 (1) (1) P-0201 A/B shut off pressure
PRO-02-0113-L3A1F-12"- F-0201 B PRO-0115 HC 30.4 40 L 373 843 706.2 0.35 35.3 85 40S 0.66 2.02
PRO-02-0114-L3A1F-12"- F-0201 A PRO-0113 HC 30.4 40 L 373 843 706.1 0.35 35.3 85 40 0.68 2.04
PRO-02-0115-L3C1F- 18"- PRO-0113 E-0201 H2O + H2S + H2 +HC
29.0 41 MLV
385 609376 167
9 442
151.4699.64.701
0.320.010
35.3 85 (435) 0.54 4.76 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 5 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 01/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/3
8/3/2019 LIS-OO-0003-0
5/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0116-L6C1F-24"-H
E-0201 H-0201 H2O + H2S + H2 +HC
27.9 298 V 385 749 41.57 0.016 33.9 323 40 0.42 9.93 PWHT
PRO-02-0117-B3B3F- 8"-P E-0201 PRO-0113 H2O + H2S + H2 +
HC
29.1 68 V 11 906 5.155 0.011 35.3 93 40 0.74 19.9 PWHT
PRO-02-0118-B3C3F-20"-P
E-0201 E-0202 H2O + H2S + H2 +HC
21.9 95 MLV
385 750359 34726 403
101.3654.18.101
0.220.014
26.7 133 40 0.49 5.90 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0119-A3A3F-6"- PRO-0110 FV-02-001 HC 36.4 40 L 112 153 707.7 0.35 46.9(1)
85 40 21.73 2.36 Pump mini-flow line(1) (1) P-0201 A/B shut off pressure
PRO-02-0120-A1A3F-6"- FV-02-001 PRO-0102 HC 2.5 40 L 112 153 702.7 0.34 4.5 85 40 21.88 2.38 Pump mini-flow line
PRO-02-0121-A3A3F-12"- Storage FV-02-004 HC 6.0 40 L 373 880 703.3 0.34 8.0 85 40 0.68 2.05 NNF
PRO-02-0122-A1A3F-12"- FV-02-004 PRO-0102 HC 2.5 40 L 373 843 702.7 0.34 4.5 85 40 0.68 2.05
PRO-02-0123-A1A3F-8"- PRO-0111 E-0207 HC 30.1 40 L 224 306 706.1 0.35 46.9(1)
85 40 5.29 2.73 Start-up line(1) (1) P-0201 A/B shut off pressure
PRO-02-0124-M1F1-1 1/2"- PRO-0702 P-5201 A/B Sulf. Ag. NNF
PRO-02-0125-M1F1-1 1/2"- PRO-0702 P-7201 A/B Sulf. Ag. NNF
PRO-02-0126-L6C1F PRO-0202 PRO-0116 CO2+N2+H2O+AIR
5.7 149.8 V 25000 5.431 0.023 9.2 175 40 0.38 17.5 E-0201 by-pass line used only duringcatalyst regeneration
FL-02-0101-A1A3F-4"- FLG PV-02-005-A H2 + HC 3.9 40 V 603 1.631 0.012 5.9 85 40 0.24 12.5
FL-02-0102-A1A3F-4"- PV-02-005-A VH-0201 H2 + HC 2.5 40 V 603 1.166 0.012 4.5 85 40 0.33 17.5
FL-02-0103-A1A3F-4"- FL-0102 PV-02-005-B H2 + HC 2.5 40 V 603 1.166 0.012 4.5 85 40 0.33 17.5
FL-02-0104-A1A3F-6"- PV-02-005-B FLR 0.3 40 V 603 0.4362 0.012 3.5 85 40 0.11 20.6
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 5 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 01/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/3
8/3/2019 LIS-OO-0003-0
6/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0201-L6C1F-24"-H
H-0201 R-0201 H2O + H2S + H2 +HC
25.9 340 V 385 749 34.91 0.017 33.9 365 (584) 0.46 11.5 PWHT
PRO-02-0202-L6C1F-24"-
H
R-0201 E-0201 H2O + H2S + H2 +
HC
23.8 345 V 385 750 31.92 0.017 28.6 370 (588) 0.77 12.4 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 6 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 02/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/1
8/3/2019 LIS-OO-0003-0
7/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 9 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 03/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/3
8/3/2019 LIS-OO-0003-0
8/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0301-B3C3F-18"-P
E-0202 E-0203 H2O + H2S + H2 +HC
21.4 60 MLV
385 749370 65315 096
112.7683.65.240
0.270.012
25.9 108 40 0.77 6.59 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0302-B3C3F- 18"- E-0203 VH-0202 H2O + H2S + H2 +HC
20.8 40 MLV
385 750374 38611 364
118.2700.74.165
0.320.011
25.3 85 40 0.74 6.29 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0303-B3H3F- 10"- VH-0202 PRO-0304 H2O + H2S + H2 +HC
20.8 40 V 11 364 4.146 0.011 25.2 85 40 0.26 15.0 PWHT
PRO-02-0304-B3H3F- 10"- PRO-0303 VV-0201 H2O + H2S + H2 +HC
20.8 40 V 11 906 4.075 0.011 25.2 85 40 0.29 16.0 PWHT
PRO-02-0305-B3H3F-10"-
ST
VV-0201 C-0201 A H2O + H2S + H2 +HC
20.6 40 V 11 906 4.056 0.011 25.2 85 40 0.29 16.0 PWHT
PRO-02-0306-B3H3F-10"-
ST
PRO-0305 C-0201 B H2O + H2S + H2 +HC
20.6 40 V 11 906 4.056 0.011 25.2 85 40 0.29 16.0 PWHT
PRO-02-0307-B3H3F- 8"-P C-0201 A E-0201 H2O + H2S + H2 +
HC
29.3 68 V 11 906 5.189 0.011 35.3 93 40 0.73 19.7 PWHT
PRO-02-0308-B3H3F- 8"-P C-0201 B PRO-0307 H2O + H2S + H2 +HC
29.3 68 V 11 906 5.189 0.011 35.3 93 40 0.73 19.7 PWHT
PRO-02-0309-B3C3F-12"- VH-0202 E-0207 H2O + H2S + HC 20.8 40 L 374 386 700.7 0.32 25.5 85 40 0.68 2.06 PWHT
PRO-02-0310-A3H3F-3"- AIR BL E-0204 AIR 5.0 40 V 599 6.705 0.019 7.0 85 40 0.23 5.20
PRO-02-0311-A3H1F-3"- H2 Make-up FV-02-009 H2 30.9 32 V 542 4.391 0.0096 34.0 85 40 2.1 15.9
PRO-02-0312-B3H3F-3"- FV-02-009 PRO-0303 H2 20.8 32 V 542 3.001 0.0096 25.3 85 40 0.41 10.5 PWHT
PRO-02-0313-B3H3F-11/2"-
PRO-0303 FV-02-010 H2O + H2S + H2 +HC
20.8 40 V 81 4.127 0.011 25.3 85 80 0.29 4.77 PWHT
NNF
PRO-02-0314-B1H3F-11/2"-
FV-02-010 AMINETREATMENT
H2S + H2 + HC 7.0 40 V 81 1.539 0.011 9.0 85 80 0.79 12.8 PWHT
NNF
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 9 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 03/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/3
8/3/2019 LIS-OO-0003-0
9/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0315--- PRO-0303 EJ-0201 By EngineeringNNFPWHT
PRO-02-0316-B3C3F-11/2"- VV-0201 PRO-0404 H2O + H2S + H2 +HC 25.2 162 NNFPWHT
ATM-02-0301-A1V3F-4"- PRO-0314 ATM N2 + CO2 + H2O +Ar
0.0 33 V 489 0.9357 0.018 3.5 85 40 0.29 17.7
ATM-02-0302--- EJ-0201 ATM By Engineering
BFW-02-0302-M3L1F-3"-P FV-02-007 PRO-0118 H2O 21.9 130 L 18 694 934.8 0.21 26.7 165 40 1.5 1.16
CAU-02-0302-M1L1F-11/2"-
FV-02-008 MX-0201 NaOH + H2O 6.0 30 L 3 886 1 026 1.5 7.0 85 40S 2.22 0.799 PWHT
FL-02-0301--- PRO-0303 FLARE H2 + HC (C)
Depressurization line
SWA-02-0301-B3L3F-3"- VH-0202 LV-02-005 H2O + H2S + HC 20.8 40 L 18 694 992.1 0.65 25.5 85 40 1.55 1.10 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 9 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 03/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/3
8/3/2019 LIS-OO-0003-0
10/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
SWA-02-0302-B1L3F-3"- LV-02-005 SWA-0304 H2O + H2S + HC 5.0 41 L 18 694 991.9 0.65 7.0 85 40 1.55 1.10 PWHT
SWA-02-0303-B1L3F-2"- SWA-0302 SPENTCAUSTIC
NaOH + H2O 2.5 35 L 6 292 1 021 0.81 4.5 85 40 1.44 0.791 NNF
SWA-02-0304-B1L3F-3"- SWA-0302 SOUR WATERSTRIPPER UNIT
H2O + H2S + HC 5.0 41 L 18 706 991.9 0.65 7.0 85 40 1.55 1.10 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 9 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 03/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 4/3
8/3/2019 LIS-OO-0003-0
11/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 13 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 04/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/4
8/3/2019 LIS-OO-0003-0
12/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0401-B3C3F-12"-H
E-0207 E-0204 H2O + H2S + HC 20.1 90 L 374 386 654.3 0.22 22.1 115 40 0.72 2.20 PWHT
PRO-02-0402-B3C3F-12"-H
E-0204 FV-02-012 H2O + H2S + HC 19.4 137 L 374 386 602.0 0.14 21.4 162 40 0.76 2.39 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0403-B1C3F-10"-H
FV-02-012 PRO-0404 H2O + H2S + HC 9.8 137 MLV
374 386368 843
5 543
387.8605.615.55
0.150.013
11.8 162 40 2.93 5.27 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0404-B1C3F- 8"-H PRO-0403 CC-0201 H2O + H2S + HC 9.8 137 MLV
187 194184 422
2 772
387.7605.615.55
0.150.013
11.8 162 40 9.47 4.15 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0405-B1C3F- 8"-H PRO-0403 CC-0201 H2O + H2S + HC 9.8 137 MLV
187 194184 422
2 772
387.7605.615.55
0.150.013
11.8 162 40 9.47 4.15 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0406-B1C3F-12"-
P
CC-0201 E-0205 H2O + H2S + HC 9.7 101 V 109 736 24.65 0.010 11.7 126 40 1.56 17.1 Piping diameter to be checked by
ODCC/EIL according to flowrate at PSVrelieving conditionsPWHT
PRO-02-0407-B1C3F- 8"-P E-0205 E-0206 H2O + H2S + HC 9.2 60 MLV
109 73798 18711 550
117.4558.915.22
0.130.011
11.7 101 40 2.77 8.04 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0408-B1C3F- 8"- E-0206 VH-0203 H2O + H2S + HC 8.9 40 MLV
109 736105 001
4 735
182.6583.611.25
0.160.011
11.7 85 40 1.79 5.17 PWHTTwo phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0409-B1B3F-10"- VH-0203 P-0202 A H2O + H2S + HC 8.9 40 L 104 828 583.2 0.15 12.1 85 40 0.16 0.982 PWHT
PRO-02-0410-B1B3F-10"- PRO-0409 P-0202 B H2O + H2S + HC 8.9 40 L 104 828 583.2 0.15 12.1 85 40 0.16 0.982 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 13 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 04/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/4
8/3/2019 LIS-OO-0003-0
13/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0411-B3B3F- 8"- P-0202 A FV-02-016 H2O + H2S + HC 15.8 40 L 104 828 584.3 0.16 20.1(1)
85 40 0.51 1.54 PWHT(1) P-0202 A/B shut-off pressure
PRO-02-0412-B3B3F- 8"- P-0202 B PRO-0411 H2O + H2S + HC 15.8 40 L 104 828 584.3 0.16 20.1(1)
85 40 0.51 1.54 PWHT(1)
P-0202 A/B shut-off pressurePRO-02-0413-B1B3F-8"- FV-02-016 C-0201 H2O + H2S + HC 9.7 40 L 104 828 583.2 0.15 11.7 85 40 0.51 1.55 PWHT
PRO-02-0414-B1B3F-4"- VH-0203 PV-02-035 H2O + H2S + HC 8.9 40 V 4 781 11.24 0.011 11.7 85 40 1.9 14.4 PWHT
PRO-02-0415-B1B3F-4"- PV-02-035 AMINETREATMENT
H2O + H2S + HC 7.0 39 V 4 781 9.073 0.011 9.0 85 40 2.36 17.8 PWHT
PRO-02-0416-A1A3F-24"-H
C-0201 PRO-0425 HC 10.8 184 L 891 634 550.4 0.11 13.3 209 40 0.17 1.73
PRO-02-0417-A1A3F-20"-H
PRO-0416 P-0205 A HC 10.8 184 L 522 157 550.4 0.11 13.3 209 40 0.16 1.47
PRO-02-0418-A1A3F-20"-H
PRO-0417 P-0205 B HC 10.8 184 L 522 157 550.4 0.11 13.3 209 40 0.16 1.47
PRO-02-0419-A3A3F-16"-
H
P-0205 A FV-02-017 HC 16.6 184 L 522 157 553.4 0.11 20.7
(1)
209 40 0.49 2.30 (1) P-0205 A/B shut-off pressure
PRO-02-0420-A3A3F--H P-0205 B PRO-0419 HC 16.6 184 L 522 157 553.4 0.11 20.7(1)
209 40 0.49 2.30 (1) P-0205 A/B shut-off pressure
PRO-02-0421-A3A3F-16"-H
FV-02-017 H-0202 HC 12.2 184 L 14.6 209 By Engineering
PRO-02-0422-A1A3F--H H-0202 PRO-0423 HC 10.2 206 MLV
12.7 231 STD 0.31 7.34 Two phase flow: provide appropriatesupport to prevent from vibrations
By Engineering
PRO-02-0423-A1A3F-20"-H
PRO-0422 CC-0201 HC 10.2 206 MLV
261 079130 539
130 540
61.27553.732.43
0.110.011
12.7 231 40 0.36 6.60 Two phase flow: provide appropriatesupport to prevent from vibrations
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 13 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 04/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/4
8/3/2019 LIS-OO-0003-0
14/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0424-A1A3F-20"-H
PRO-0422 CC-0201 HC 10.2 206 MLV
261 079130 539
130 540
61.27553.732.43
0.110.011
12.7 231 40 0.36 6.60 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0425-A1A3F-12"-H
PRO-0416 E-0204 HC 10.8 184 L 369 477 550.4 0.11 12.8 209 40 0.81 2.58
PRO-02-0426-A1A3F-12"-P
E-0204 FV-02-019 HC 10.1 139 L 369 477 607.2 0.15 12.8 164 40 0.74 2.34
PRO-02-0427-A3A3F-10"-H
E-0207 OCTANIZERUNIT
HC 10.3 92 L 217 093 695.7 0.29 19.5 (1) 117 40 0.58 1.70 (1) Estimated shut-off pressure of P-0207A/B
PRO-02-0428-B3B3F-11/2"-
PRO-0411 PRO-0705 H2O + H2S + HC 15.8 40 L 10 584.3 0.16 20.1
(1)
85 80
8/3/2019 LIS-OO-0003-0
15/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
HYD-02-0401--- H2 PRO-0414 H2 (C)Start-up line
SWA-02-0401-B1L3F-11/2"-
VH-0203 SWA-0302 H2O + H2S + HC 8.9 40 L 128 992.1 0.65 12.3 85 40
8/3/2019 LIS-OO-0003-0
16/31
8/3/2019 LIS-OO-0003-0
17/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(1)
PRO-02-0515-A1A3F-4"- PRO-0514 TO LPG MEROXUNIT
HC 9.7 40 L 21 156 798.3 0.86 15.1(1)
85 40 2.5 1.54 (1) P-0211 A/B shut-off pressure
PRO-02-0516-A1A3F-4"- FV-02-027 GASOLINEPOOL
HC 6.0 40 L 21 156 797.8 0.85 15.1(1)
85 40 0.65 0.897 (1) P-0211 A/B shut-off pressure
PRO-02-0517-A1A3F-10"-P
VV-0202 CC-0202 HC 2.6 172 V 39 618 37.66 1.0 4.7 197 40 0.52 5.75 Piping diameter to be checked byEngineering according to f lowrate at PSVrelieving conditions
PRO-02-0518-A3A3F-3"- PRO-0514 PRO-0519 HC 9.7 40 L 12 694 798.3 0.86 19.5(1)
85 40 0.96 0.926 NNFStart-up line
(1) P-0207 A/B shut-off pressure
PRO-02-0519-A3A3F-6"-P PRO-0506 PRO-0101 HC 10.3 92 L 130 256 695.7 0.29 19.5(1)
117 40 7.52 1.61 NNFStart-up line
(1) P-0207 A/B shut off pressure
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 16 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 05/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/3
8/3/2019 LIS-OO-0003-0
18/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 16 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 05/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/3
8/3/2019 LIS-OO-0003-0
19/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
CWR-02-0401-ByEng-4"- E-0211 CWR H2O 3.0 40 L 43 200 992.0 0.65 7.0 65 40 1.22 2.06
CWS-02-0401-ByEng-4"- CWS E-0211 H2O 4.0 35 L 43 200 994.0 0.72 7.0 65 40 1.23 2.06
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 16 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 05/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 4/3
8/3/2019 LIS-OO-0003-0
20/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/5
8/3/2019 LIS-OO-0003-0
21/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0601-A1A3F-18"-H
FV-02-019 PRO-0602 HC 2.2 124 MLV
369 478317 14952 329
58.19634.08.947
0.190.0091
4.5 149 40 1.34 12.2 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0602-A1A3F-10"-H
PRO-0601 CC-0202 HC 2.2 124 MLV
92 36979 28713 082
58.20634.08.947
0.190.0091
4.2 149 40 19.14 8.67 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0603-A1A3F-10"-H
PRO-0601 C-0202 HC 2.2 124 MLV
92 36479 28413 080
58.20634.08.947
0.190.0091
4.2 149 40 19.14 8.67 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0604-A1A3F-12"-H
PRO-0601 PRO-0605 HC 2.2 124 MLV
184 740158 57526 165
58.19634.08.947
0.190.0091
4.2 149 40 7.79 12.2 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0605-A1A3F-10"-H
PRO-0604 CC-0202 HC 2.2 124 MLV
92 36979 28713 082
58.20634.08.947
0.190.0091
4.2 149 40 19.14 8.67 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0606-A1A3F-10"-H
PRO-0603 CC-0202 HC 2.2 124 MLV
92 36979 28713 082
58.20634.08.947
0.190.0091
4.2 149 40 19.14 8.67 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0607-A1A3F-36"- CC-0202 PV-02-090 HC 2.0 92 V 374 960 8.518 0.0086 4.0 117 40 0.22 20.3
PRO-02-0608-A1A3F-36"- PV-02-090 E-0208 HC 1.4 91 V 374 960 6.725 0.0085 3.5 117 STD 0.25 24.6
PRO-02-0609-A1A3F-16"- E-0208 VH-0204 HC 1.1 50 L 374 960 632.2 0.22 3.5 85 40 0.23 1.45
PRO-02-0610-A1A3F-16"- VH-0204 PRO-0612 HC 1.0 50 L 374 960 632.1 0.22 3.8 85 40 0.23 1.45
PRO-02-0611-A1A3F-12"- PRO-0611 P-0203 A HC 1.0 50 L 243 732 632.1 0.22 3.8 85 40 0.32 1.48
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/5
8/3/2019 LIS-OO-0003-0
22/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0612-A1A3F-12"- PRO-0612 P-0203 B HC 1.0 50 L 243 732 632.1 0.22 3.8 85 40 0.32 1.48
PRO-02-0613-A1A3F-12"- P-0203 A FV-02-029 HC 9.0 50 L 243 732 632.8 0.22 13.3(1)
85 40 0.78 2.10 (1) P-0203 A/B shut-off pressure
PRO-02-0614-A1A3F-12"- P-0203 B PRO-0613 HC 9.0 50 L 243 732 632.8 0.22 13.3(1)
85 40 0.78 2.10 (1) P-0203 A/B shut-off pressure
PRO-02-0615-A1A3F-12"- FV-02-029 CC-0202 HC 2.0 50 L 243 732 632.3 0.22 4.0 85 40 0.78 2.11
PRO-02-0616-A1A3F-6"- PRO-0607 PV-02-089 HC 2.0 92 V 3 432 8.518 0.0086 4.0 117 40 0.34 8.84
PRO-02-0617-A1A3F-6"- PV-02-089 VH-0204 HC 1.0 78 V 3 432 5.786 0.0082 3.5 103 40 0.23 8.84
PRO-02-0618-A1A3F-- PRO-0609 VH-0204 HC 1.1 50 L (C) (C) (C) 3.5 85 Equalizing line Line diameter to bedefined by Engineering
PRO-02-0619-A1A3F-12"- PRO-0610 P-0209 A HC 1.0 50 L 131 228 632.1 0.22 3.8 85 40 0.1 0.799
PRO-02-0620-A1A3F-12"- PRO-0619 P-0209 B HC 1.0 50 L 131 228 632.1 0.22 3.8 85 40 0.1 0.799
PRO-02-0621-A1A3F-8"- P-0209 A E-0209 HC 11.7 50 L 131 228 633.8 0.22 16.5(1) 85 40 0.74 1.78(1)
P-0209 A/B shut-off pressure
PRO-02-0622-A1A3F-8"- P-0209 B PRO-0621 HC 11.7 50 L 131 228 633.8 0.22 16.5(1)
85 40 0.74 1.78 (1) P-0209 A/B shut-off pressure
PRO-02-0623-A1A3F-8"- E-0209 FV-02-035 HC 11.2 40 L 131 228 643.7 0.24 16.5(1)
85 40 0.74 1.75 (1) P-0209 A/B shut-off pressure
PRO-02-0624-A1A3F-8"- FV-02-035 ISOM UNIT HC 7.5 40 L 131 228 643.0 0.24 16.5(1)
85 40 0.74 1.76 (1) P-0209 A/B shut-off pressure
PRO-02-0625-A1A3F-8"- PRO-0623 FV-02-034 HC 11.2 40 L 131 228 643.7 0.24 16.5(1)
85 40 0.74 1.75 NNF(1) P-0209 A/B shut-off pressure
PRO-02-0626-A1A3F-8"- FV-02-034 STORAGE HC 6.0 40 L 131 228 643.0 0.24 16.5(1)
85 40 0.74 1.76 NNF(1) P-0209 A/B shut-off pressure
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/5
8/3/2019 LIS-OO-0003-0
23/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0627-A1A3F-26"-H
CC-0202 PRO-0628 HC 2.7 247 L 1 135 674 624.0 0.15 6.0 272 STD 0.14 1.57
PRO-02-0628-A1A3F-26"-H
PRO-0627 PRO-0629 HC 2.7 247 L 1 114 518 624.0 0.15 6.0 272 STD 0.14 1.54
PRO-02-0629-A1A3F-20"-H
PRO-0628 P-0204 A HC 2.7 247 L 557 259 624.0 0.15 6.0 272 40 0.16 1.38
PRO-02-0630-A1A3F-20"-H
PRO-0628 P-0204 B HC 2.7 247 L 557 259 624.0 0.15 6.0 272 40 0.16 1.38
PRO-02-0631-A1A3F-20"-H
PRO-0628 P-0204 C HC 2.7 247 L 557 259 624.0 0.15 6.0 272 40 0.16 1.38
PRO-02-0632-A3A3F-16"-H
P-0204 A PRO-0635 HC 9.2 247 L 557 259 625.4 0.15 13.5(1)
272 40 0.99 2.84 (1) P-0204 A/B/C shut-off pressure
PRO-02-0633-A3A3F-16"-H
P-0204 B PRO-0635 HC 9.2 247 L 557 259 625.4 0.15 13.5(1)
272 40 0.99 2.84 (1) P-0204 A/B/C shut-off pressure
PRO-02-0634-A3A3F-16"-H
P-0204 C PRO-0635 HC 9.2 247 L 557 259 625.4 0.15 13.5(1)
272 40 0.99 2.84 (1) P-0204 A/B/C shut-off pressure
PRO-02-0635-A3A3F-20"-H
PRO-0632 FV-02-028 HC 5.7 247 L 1 114 518 625.4 0.15 13.5(1)
272 40 0.61 2.76 (1) P-0204 A/B/C shut-off pressure
PRO-02-0636-A1A3F--H FV-02-028 H-0203 HC 4.7 247 L 1 114 518 625.0 0.15 7.2 272 STD 0.33 2.16 Piping diameter to be defined byEngineering
PRO-02-0637-A1A3F--H H-0203 PRO-0638 HC 2.7 252 MLV
1 114 518557 260
557 258
27.16633.413.88
0.150.0097
7.2 277 (1154)
0.16 10.9 Two phase flow: provide appropriatesupport to prevent from vibrations
Piping diameter to be defined byEngineering
PRO-02-0638-A1A3F-32"-H
PRO-0637 CC-0202 HC 2.7 252 MLV
557 259278 630
278 629
27.16633.413.88
0.150.0097
5.3 277 40 0.31 12.0 Two phase flow: provide appropriatesupport to prevent from vibrations
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 4/5
8/3/2019 LIS-OO-0003-0
24/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0639-A1A3F-32"-H
PRO-0637 CC-0202 HC 2.7 252 MLV
557 259278 630
278 629
27.16633.413.88
0.150.0097
5.3 273 STD 1.06 11.5 Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0640-A1A3F-6"-P PRO-0627 P-0211 A HC 2.7 247 L 21 156 624.0 0.15 6.0 272 40 0.7 1.15
PRO-02-0641-A1A3F-12"-H
CC-0202 PRO-0643 HC 2.6 172 L 119 401 614.8 0.16 5.3 197 40 0.63 0.747
PRO-02-0642-A1A3F-12"-H
CC-0202 PRO-0643 HC 2.6 172 L 119 401 614.8 0.16 5.3 197 40 0.63 0.747
PRO-02-0643-A1A3F-12"-H
PRO-0642 FV-02-025 HC 2.6 172 L 217 093 614.8 0.16 5.3 197 40 0.26 1.36
PRO-02-0644-A1A3F-4"-P PRO-0627 VV-0202 HC 2.7 247 L 624.0 0.15 6.0 272 NNFStart-up line
PRO-02-0645-A1A3F-12"-P
PRO-0601 PRO-0427 HC 2.2 124 MLV
221 686190 28931 397
58.20634.08.947
0.190.0091
7.5 149 40 2.87 14.7 NNFStart-up line
CWR-02-0601-ByEng-6"- CWS E-0209 H2O 3.0 40 L 146 600 992.1 0.65 7.0 65 40 2.54 2.20
CWS-02-0601-ByEng-6"- E-0209 CWR H2O 4.0 35 L 146 600 994.0 0.72 7.0 65 40 2.56 2.20
FL-02-0601-A1A3F-6"- VH-0204 PV-02-052 HC 1.0 50 V 1 246 2.100 0.019 3.5 85 40 0.1 8.84
FL-02-0602-A1A3F-6"- PV-02-052 FLR HC 0.3 50 V 1246 1.370 0.019 3.5 85 40 0.13 12.7
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 5/5
8/3/2019 LIS-OO-0003-0
25/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
NIT-02-0601-A1A3F-- NIT VH-0204 N2 1.0 50 V 12.5 75 By Engineering
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 21 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 06/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 6/5
8/3/2019 LIS-OO-0003-0
26/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 24 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 07/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/3
8/3/2019 LIS-OO-0003-0
27/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0701-M1F1F-11/2"-
VV-0203 P-0208 A/S Sulf. Ag. 0.4 40 L 863 1 039 0.10 3.5 85 40
PRO-02-0702-M1F1F-11/2"-
P-0208 A/S PRO-0103 Sulf. Ag. 3.5 40 L 863 1 039 0.10 5.5 (1) 85 40 0.08 0.169 (1) PSV set pressure
PRO-02-0703-M1L1F-11/2"-
CORROSIONINHIBITORDRUM
P-0206 A Corr. Inhibitor 0.0 40 L 11 900.0 0.46 3.5 85
PRO-02-0704-M1L1F-11/2"-
PRO-0703 P-0206 B Corr. Inhibitor 0.0 40 L 11 900.0 0.46 3.5 80
PRO-02-0705-M1L1F-11/2"-
P-0206 A PRO-0406 Corr. Inhibitor 14.3 40 L 11 900.0 0.46 16.3(1)
85 5S (1) PSV set pressure
PRO-02-0706-M1L1F-11/2"-
P-0206 B PRO-0705 Corr. Inhibitor 14.3 40 L 11 900.0 0.46 16.3(1)
85 5S (1) PSV set pressure
BFW-02-0701-M3L1F-3"-P STRIPPEDWATER
LV-02-028-A H2O 11.0 130 L 18 694 934.8 0.21 17.0 165 5S 0.98 0.986 NNF
BFW-02-0702-M3L1F-3"-P BOILER FEEDWATER
LV-02-028-B H2O 11.0 130 L 18 694 934.8 0.21 17.0 165 5S 0.98 0.986 NNF
BFW-02-0703-M1L1F-3"-P LV-02-028-B BFW-0704 H2O 2.2 130 L 18 696 934.8 0.21 4.2 155 5S 0.98 0.986 NNF
BFW-02-0704-M1L1F-3"-P LV-02-028-A VV-0204 H2O 2.2 130 L 18 694 934.8 0.21 4.2 155 5S 0.98 0.986 NNF
BFW-02-0705-M1L1F-4"-P VV-0204 P-0210 A H2O 2.2 130 L 18 694 934.8 0.21 4.5 155 5S 0.04 0.267
BFW-02-0706-M3L1F-3"-P P-0210 A FV-02-007 H2O 28.0 130 L 18 694 934.8 0.21 35.6(1)
155 (108) 0.28 0.603 (1) P-0210 A shut-off pressure
CAU-02-0701-M1L1F-11/2"-
BL FV-02-008 NaOH 6.0 30 L 3 886 1 026 1.5 11.0 85 5S 1.4 0.662 PWHT
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 24 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 07/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/3
8/3/2019 LIS-OO-0003-0
28/31
8/3/2019 LIS-OO-0003-0
29/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 26 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 09/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 1/2
8/3/2019 LIS-OO-0003-0
30/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
PRO-02-0901-B3C3F-12"-P
PRO-0301 E-0203 A H2O + H2S +H2 + HC
21.4 60 MLV
128 583123 551
5 032
112.7683.65.240
0.270.012
25.9 108 40 4.44 4.39 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0902-B3C3F-12"-P
PRO-0301 E-0203 B H2O + H2S +H2 + HC
21.4 60 MLV
128 583123 551
5 032
112.7683.65.240
0.270.012
25.9 108 40 4.44 4.39 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0903-B3C3F-12"-P
PRO-0301 E-0203 C H2O + H2S +H2 + HC
21.4 60 MLV
128 583123 551
5 032
112.7683.65.240
0.270.012
25.9 108 40 4.44 4.39 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0904-B3C3F- 12"- E-0203 C PRO-0302 H2O + H2S +H2 + HC
20.8 40 MLV
128 583124 795
3 788
118.2700.74.165
0.320.011
25.3 85 40 4.27 4.18 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0905-B3C3F- 12"- E-0203 B PRO-0302 H2O + H2S +H2 + HC
20.8 40 MLV
128 583124 795
3 788
118.2700.74.165
0.320.011
25.3 85 40 4.27 4.18 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0906-B3C3F- 12"- E-0203 A PRO-0302 H2O + H2S +H2 + HC
20.8 40 MLV
128 583124 795
3 788
118.2700.74.165
0.320.011
25.3 85 40 4.27 4.18 PWHT
Two phase flow: provide appropriatesupport to prevent from vibrations
PRO-02-0907-A3A3F-6"-P PRO-0507 E-0213 A HC 9.8 60 L 108 547 722.0 0.38 19.5(1) 92 40 1.89 2.24 (1) P-0207 A/B shut-off pressurePRO-02-0908-A3A3F-6"-P PRO-0507 E-0213 B HC 9.8 60 L 108 547 722.0 0.38 19.5(1) 92 40 1.89 2.24 (1) P-0207 A/B shut-off pressure
PRO-02-0909-A3A3F-6"- E-0213 B PRO-0508 HC 9.5 40 L 108 547 737.5 0.46 19.5(1) 85 40 7.21 1.27 (1) P-0207 A/B shut-off pressure
PRO-02-0910-A3A3F-6"- E-0213 A PRO-0508 HC 9.5 40 L 108 547 737.5 0.46 19.5(1) 85 40 7.21 1.27 (1) P-0207 A/B shut-off pressure
CWR-02-0901-ByEng-8"- E-0203 A SWR H2O 3.0 40 L 314 400 992.1 0.65 7.0 65 40 2.76 2.73
CWR-02-0902-ByEng-8"- E-0203 B SWR H2O 3.0 40 L 314 400 992.1 0.65 7.0 65 40 2.76 2.73
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 26 OF35
Process licensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 09/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 2/2
8/3/2019 LIS-OO-0003-0
31/31
NATIONAL IRANIAN OIL ENGINEERING &CONSTRUCTION COMPANY (NIOEC)
Line Number Location Flowing conditionsProperties at
flowingconditions
DesignConditions
(B)Sch.or
Pres.drop
Velo-city
Notes
From To Nature of fluidPress.gage Temp. State
Massflow rate De ns ity Visc .
Press.gage Temp.
int
bar C (A) kg/h kg/m3 mPa.s bar C bar/km m/s
CWR-02-0903-ByEng-8"- E-0203 C SWR H2O 3.0 40 L 314 400 992.1 0.65 7.0 65 40 2.76 2.73
CWR-02-0904-ByEng-8"- E-0213 A SWR H2O 3.0 40 L 226 750 992.1 0.65 7.0 65 40 1.47 1.97
CWR-02-0905-ByEng-8"- E-0213 B SWR H2O 3.0 40 L 226 750 992.1 0.65 7.0 65 40 1.47 1.97
CWS-02-0901-ByEng-8"- SWS E-0203 A H2O 4.0 35 L 314 400 994.0 0.72 7.0 65 40 2.76 2.73
CWS-02-0902-ByEng-8"- SWS E-0203 B H2O 4.0 35 L 314 400 994.0 0.72 7.0 65 40 2.76 2.73
CWS-02-0903-ByEng-8"- SWS E-0203 C H2O 4.0 35 L 314 400 994.0 0.72 7.0 65 40 2.76 2.73
CWS-02-0904-ByEng-8"- SWS E-0213 A H2O 4.0 35 L 226 750 994.0 0.72 7.0 65 40 1.47 1.97
CWS-02-0905-ByEng-8"- SWS E-0213 B H2O 4.0 35 L 226 750 994.0 0.72 7.0 65 40 1.47 1.97
(A) L = Liquid, V = Va por , M = Mixe d pha se (B) Used for pre ssure drop a nd ve loc ity ca lc ula tion . To be che cke d by Enginee ring con tra ctor. (C) By Engine er ing (D) By Ma nufac tu re r
OIL DESIGN & CONSTRUCTION
COMPANY(OD&CC) (EIL)
OD&CC JOB No. DOC No. REV. SHEETNIOEC Job N.: 226210 RF-01 02/EB-PR/LIS-OO-0003-0 0 26 OF35
Processlicensin
Project : BANDAR ABBAS GAS CONDENSATE REFINERY PROJECT Date By Check By Rev PIPING PROCESS DATA SHEETUnit :
P&ID :
NAPHTHA HYDROTREATERPID 09/09
12/05/2006 JSI GBR 0 Job Number U nit Type Page
04-2501 02 3PI 3/2