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