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LIS-OO-0003-0

Apr 06, 2018

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  • 8/3/2019 LIS-OO-0003-0

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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

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    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