2014-4825-9m-0001 rev f process datasheet for production separator

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  • Rev:

    SU TU TRANG FULL FIELD DEVELOPMENT PHASE 1

    DETAILED ENGINEERING AND PROCUREMENT ENGINEERING SUPPORT SERVICES

    PROCESS DATASHEET FOR PRODUCTION SEPARATORDoc. No.: 2014-4825-9M-0001

    F

    REVISION RECORD SHEET

    No. Rev. No Content of Revision Date of Revision1 D Approved for Design (FEED) 15-01-15

    2 EIssued for Review:- Add Turndown Case.- Add Note 17, revise Note 2, 9, 16.

    22-05-15

    3 F Issued for Approval 28-05-15

    Page No.: 2 of 5

  • PROCESS DATA SHEET

    4825 9M F

    CLIENT Rev. Date Made by Checked by Page

    LOCATION

    UNIT

    1

    2345678 FLUID9

    101112 OPERATING CASE MAX OIL CASE MAX GAS CASE TURNDOWN CASE131415 FLUID QUALITY1617 TEMPERATURE C 80 118 1181819 PRESSURE kPag 9130 9130 91302021 ALLOWABLE PRESSURE DROP kPa 20 (NOTE 3) 20 (NOTE 3) 20 (NOTE 3)2223 GAS2425 FLOW RATE kg/h 170789.8 (NOTE 6) 195344.2 (NOTE 6) 69994.6 (NOTE 6)2627 MOLECULAR WEIGHT 21.67 23.49 23.4862829 DENSITY UNDER CONDITIONS kg/m 82.19 77.35 77.3553031 LIQUID3233 FLOW RATE kg/h 157433.1 124363.9 445613435 DENSITY (OIL / WATER) kg/m 605.05 / 968.02 606.35/ 936.97 606.35/ 936.973637 SURFACE TENSION (OIL/ WATER) dyne/cm 8.75 / 62.34 8.86/ 55.13 8.86/ 55.133839 VISCOSITY (OIL / WATER) cP 0.27 / 0.35 0.26/ 0.23 0.26/ 0.23404142 DESIGN CONDITIONS4344 TEMPERATURE C4546 PRESSURE kPag (psig)4748 MATERIAL SHELL49 INTERNAL50 CORROSION ALLOWANCE SHELL mm51 INTERNAL mm52 INSULATION/TRACING5354 HEADS TYPE5556 NOTES57 VTA: Vendor to Advise58 VTC: Vendor to confirm59 Refer to page 4/5 for Notes and Holds6061626364656667686970717273

    Rev.

    2014Project No.-Unit

    MBD-2902Fcl./Syst. Code Doc. Type Serial No. Equiment No.

    0001

    NIL

    -28 / 130

    13000 (1885)

    YES (PERSONNEL PROTECTION) (NOTE 12)

    CS + SS316L Cladding (NOTE 5) SS316L

    3.0

    ELLIPTICAL (VTC)

    Production Separator

    TYPE

    SERVICE

    3/5

    22-05-15TM

    DIMENSIONS 2600 mm I.D. x 9000 mm T/T (NOTE 1)

    ST-PIP

    Horizontal Separator (NOTE 8)

    ITEM

    EPRODUCTION SEPARATOR

    CUU LONG JOC

    SU TU TRANG DVL

    MBD - 2902

    HC Gas + Liquid and Water

    Rev

    isio

    n

    F 28-05-15DVL TM

  • PROCESS DATA SHEET Rev.

    F

    CLIENT Rev.

    LOCATION

    UNIT

    12 NOTES:3 1) VENDOR SHALL ADVISE ANY MINIMUM STRAIGHT LENGTH REQUIRED FOR INLET PIPE AND OUTLET PIPE (IF ANY)4 2) VESSEL INTERNALS SHALL BE DESIGNED FOR ALL THE GIVEN CASES OF OPERATION. ADDITIONALLY 25% TURNDOWN ON 5 MAX GAS CASE SHALL BE PROVIDED.6 3) MAXIMUM ALLOWABLE PRESSURE DROP (INCLUDING ALL INTERNALS). VENDOR TO ADVISE ACTUAL PRESSURE DROP7 FOR ALL CASES OF OPERATION.8 4) REQUIRED PERFORMANCE SPECIFICATION FOR VESSEL & INTERNALS:9 a) REMOVAL OF 99% OF ALL PARTICLES ABOVE 10m FROM VAPOUR

    10 b) MAXIMUM LIQUID CARRY OVER OF 0.1 GAL/ MMSCF11 5) MATERIAL SHALL BE IN COMPLIANCE WITH NACE MR-0175 / ISO 1515612 6) 10% ADDITIONAL MARGIN ON FLOW SHALL BE CONSIDERED FOR DESIGN OF INTERNALS13 7) VENDOR SHALL CONFIRM THE DIAMETER & VESSEL LENGTH BASED ON INTERNALS SELECTED & REQUIRED PERFORMANCE14 AS A MINIMUM SIZES GIVEN IN DATASHEETS SHALL BE MAINTAINED.15 8) INTERNAL DEVICES TO BE ADVISED BY VENDOR. AS A MINIMUM THE FOLLOWING IS ENVISAGED16 a) VANE PACK FOR MIST ELIMINATION OR EQUIVALENT17 b) VANE TYPE INLET DEVICE OR EQUIVALENT18 c) VORTEX BREAKER FOR OUTLET LIQUID NOZZLE19 9) VENDOR SHALL CONFIRM THE HEIGHT AND LENGTH OF VANE TYPE INLET DEVICE. VENDOR SHALL PROVIDE THE FEED NOZZLE 20 LOCATION BASED ITS DESIGN OF INLET DEVICE & MINIMUM CLEARANCES INDICATED IN SKETCH ON SHT 5 OF 5. 21 VENDOR SHALL ALSO PROVIDE THE VANE PACK MIST ELIMINATOR DIMENSIONS AND LOCATION OF GAS OUTLET NOZZLE.22 10) UTILITY CONNECTION FOR FLUSHING AND CLEANING.23 11) NOZZLE LOCATION AND ORIENTATION ARE INDICATIVE ONLY.24 12) VESSEL SHALL BE HEAT TRACED AT BOTTOM TILL LALL.25 13) VANE TYPE INLET DEVICE TO BE LOCATED MINIMUM150 MM FROM CONDENSATE HIGH HIGH LEVEL SET POINT.26 14) VORTEX BREAKER ELEVATED MINIMUM 150 MM TO MINIMISE SAND CARRY OVER.27 15) PROCESS FLUID MAY CONTAIN THE FOLLOWING CONTAMINANTS:28 H2S: 50 PPMV GAS PHASE & 50 - 175 PPM WT IN LIQUID PHASE29 MERCURY: 296 - 361 MICROGRAM/ NM GAS PHASE & 43 - 177 PPB WT LIQUID PHASE30 16) VENDOR SHALL CONFIRM SIZES OF FEED INLET, GAS OUTLET AND LIQUID OUTLET NOZZLE BASED ON INTERNAL OFFERED.31 AS A MINIMUM SIZES INDICATED IN DATASHEET SHALL BE FOLLOWED.32 17) VENDOR SHALL SUBMIT PERFORMANCE CALCULATIONS FOR ALL CASES OF OPERATION SHOWN INCLUDING TURNDOWN.3334353637383940414243444546

    47

    484950515253545556575859606162

    Project N - Unit Fcl./Syst. Code Doc. Type Serial No. Equipment No.

    2014 4825 9M 0001 MBD-2902

    CUU LONG JOC

    PRODUCTION SEPARATOR

    Date Made by Checked by Page

    DVL TM

    Rev

    isio

    nE 22-05-15 DVL TM

    4/ 5SU TU TRANG F 28-05-15

    ST-PIP

  • PROCESS DATA SHEETFcl./Syst. Code Doc. Type

    CLIENT Page

    LOCATION

    UNIT

    1 ITEM2 SERVICE3 OPERATING PROCESS DESIGN4567 OPERATING PROCESS DESIGN8 C C9

    1011 SHELL/ENDS1213141516 Density at T : kg/m171819 Lower TL elevation above ground = min.20 Notes :21 Refer to page 4/522 Holds :23 Refer to page 4/52425 NOZZLE DATA 26 Nb DN (mm) SERVICE27 N1 1 400 Feed Inlet (with vane type inlet device)28 N2 1 400 Gas Outlet29 N3 1 350 Liquid Outlet30 N4 1 100 Pressure Safety Valve 31 N5 1 100 Sand Jetting Supply / Drain Nozzles32 N6 1 50 Utility Connection33 N7 1 50 Vessel Vent34 N8 1 100 Sand Jetting Supply / Drain Nozzles35 N9A/B/C 3 50 Drain36 K1A/B 2 50

    37 50

    38 50 Pressure gauge

    39 50

    40 5041 600 Manway42434445464748495051525354

    55

    56

    57

    58

    59

    606162636465666768697071

    Pressure Diff. Transmitter

    K2A/B

    K3

    K5

    K6MW

    2 Level gauge & Transmitter

    1

    1

    12

    See Page 3/5

    Lining -By Mechanical

    REF.

    Level LL (Trips)

    Temperature Transmitter

    Fluid : HC Gas / Condensate / Water

    Insulation YES

    Corrosion allow. - -

    INTERNAL

    Materials CS + SS316L Cladding SS316L

    Temperature80 - 118 130/-28

    Production Separator

    Pressure bar g bar g91.3 130

    MBD - 2902

    ST-PIP Rev

    isio

    nE 22-05-15 DVL TM

    5/5SU TU TRANG F 28-05-15

    CUU LONG JOC

    PRODUCTION SEPARATOR

    Rev. Date Made by Checked by

    DVL TM

    Project No.-Unit Serial N Equipment N Rev. Index

    2014 4825 9M 0001 MBD-2902 F

    L= 90

    00 m

    m (T

    /T)

    ID =

    2600

    mm

    N2

    N7

    K6

    K3

    K1A

    N9A

    N3

    N6

    N5

    MW

    MW

    N8

    K1B

    K2A K2B

    MIN

    MIN

    150 m

    m (N

    OTE

    8b,13

    ) LA

    HH

    NOTE

    14

    N1

    150 m

    m

    N9B

    N9C

    (NOT

    E 8a

    )

    MINI

    MUM

    NOTE

    9

    NOTE

    9

    N4

    K5

    CoverChange123