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BATTERY LIMIT TABLE
Project : LDCBD5 (LOUIS DREYFUS COMMODITIES LAMPUNG)
Revision : 2
Date : 5/11/2014
FROM SOURCE TO DESTINATIONSIZE
(DN)
TIE IN
SIDE
(VIEW)
TIE IN
LEVEL
(m)
FLUIDPIPING
CLASS
INSU
LATI
ON
MIN FLOW
(kg/Hr)
OPE FLOW
(kg/Hr)
MAX FLOW
(kg/Hr)
MIN
PRESSURE
(BarG)
OPERATE
PRESSURE
(BarG)
MAX
PRESSURE
(BarG)
MIN TEMP
(°C)
OPERATE
TEMP (°C)
MAX
TEMP (°C)
OPE
DENSITY
(kg/m3)
OPE
Viscosity
(cP)
Notes
A1 RBDPO/ RBD OILS STORAGE B1 UNIT 180E1 100 5 OL C101 I1 20833 41667 50000 3 3 6 50 60 100 940 50 (3) (9)
A2 BIODIESEL STORAGE (REWORK) B2 UNIT 180E1 100 5 MH F101 I1 20833 41667 50000 3 3 6 50 60 100 860 4 (3) (9)
A3 SODIUM METHYLATE STORAGE B3 UNIT 163 CATALYST HEADER (RECIRC LOOP) 50 5 SM F101 - 3500 688 9000 4 4 6 40 50 80 960 40 (3)
A4 METHANOL STORAGE B4 UNIT 160V2 50 5 ME F101 - 5000 4021 15000 3 3 6 AMBIENT AMBIENT 60 790 0.6 (3)
A5 NITROGEN 7 BARG MAIN SUPPLY B5 ISBL NITROGEN PRV HEADER 50 4 NN C101 - 40 Nm3/Hr 40 Nm3/Hr 300 Nm3/Hr 7 7 9 AMBIENT AMBIENT 50 9 0.018
A6 MP STEAM 12 BARG MAIN SUPPLY B6 ISBL MP/ LP STEAM PRV HEADER 250 4 MS C312 I2 6250 12500 23750 12 12 15 191 191 205 6 0.015 (8)
A7 HCL STORAGE B7 UNIT 166P6 (RECIRC LOOP) 25 5 HC PV01 - 1000 2000 3000 1 2 3 AMBIENT AMBIENT 60 1100 10 (3)
A8 NAOH STORAGE B8 UNIT 166P7 (RECIRC LOOP) 25 5 NA F101 - 1000 2000 3000 3 3 6 40 50 90 1510 16 (3)
A9 CRUDE GLYCERINE STORAGE (REWORK) B9 UNIT 166V3 50 5 GR F101 I1 2604 5208 6250 3 3 6 50 60 100 1240 20 (3) (9)
A10 HOT WATER B10 SEPARATOR STARTUP & CLEANING 25 4 WH C121 I7 0 2500 5000 2 2 6 70 80 90 1000 1 (6)
A11 SOFTENED WATER B11 SEPARATOR STARTUP & CLEANING 25 4 WS C121 - 0 2500 5000 2 2 6 AMBIENT AMBIENT 50 1000 1
A12 PROCESS WATER B12 SEPARATOR & OTHER USERS 65 4 PW C121 - 100 14000 20000 3 4 6 AMBIENT AMBIENT 60 1000 1
B13 UNIT 166E3 CRUDE GLYCERINE BYPRODUCT A13 CRUDE GLYCERINE STORAGE 50 5 GR S101 I1 521 5208 6250 3 3 11 50 60 100 1240 20 (9)
B14 UNIT 166S1 FATTY MATTER BYPRODUCT A14 FATTY MATTER/ CPO STORAGE 50 5 HG S101 I1 104 208 1042 1 2 3 40 50 80 900 10
B15 UNIT 163 CATALYST HEADER (RECIRC LOOP) A15 SODIUM METHYLATE STORAGE 50 5 SM F101 - 344 688 2064 3 3 6 40 50 60 960 40
B16 UNIT 160V2 (EMPTY SYSTEM) A16 METHANOL STORAGE 50 5 ME F101 - 6320 12640 15800 3 3 6 AMBIENT AMBIENT 60 790 0.6
B17 MP STEAM CONDENSATE A17 BOILER/ TO BE SPECIFIED BY CLIENT 100 4 MC C312 I2 3000 6000 10000 10 12 12 191 191 205 900 0.13 (8)
B18 LP STEAM CONDENSATE A18 BOILER/ TO BE SPECIFIED BY CLIENT 100 4 LC C111 I1 5000 10000 15000 2 3 4 139 139 152 940 0.2 (8)
B19 ISBL CTW RETURN HEADER A19 OSBL CTW RETURN HEADER 500 4 CW C121 - 1500000 1600000 1800000 2 3 6 AMBIENT 38 60 1000 1
A20 OSBL CTW PUMP B20 ISBL CTW SUPPLY HEADER 500 4 CW C121 - 1500000 1600000 1800000 4 5 6 AMBIENT 32 38 1000 1 (10)
A21 INSTRUMENT AIR MAIN SUPPLY B21 ISBL PNEUMATIC DISTRIBUTION HEADER 50 4 IA G131 - 30 Nm3/Hr 67 Nm3/Hr 150 Nm3/Hr 6 7 9 AMBIENT 35 50 10 0.018
B22 UNIT 163E3B/C FINAL BIODIESEL A22 BIODIESEL STORAGE TANK 100 5 MH F101 I7 20833 41667 50000 3 3 6 50 60 60 860 4
B23 LIQUID EFFLUENT A23 SEWER/ FAT TRAP 150 0 WW C121 - 50 334 3336 GRAVITY GRAVITY GRAVITY 50 60 90 900 10
B24 UNIT 163S2/ 163S20 COOLING JACKET A24 COOLING TOWER BASIN 50 4 CW C121 - 50 400 2000 0.5 0.5 1 25 32 38 1000 1
A25 UNIT 166P6 (RECIRC LOOP) B25 HCL STORAGE 25 5 HC PV01 - 1000 2000 3000 1 2 3 AMBIENT AMBIENT 60 1100 10 (3)
A26 UNIT 166P7 (RECIRC LOOP) B26 NAOH STORAGE 25 5 NA F101 - 1000 2000 3000 3 3 6 40 50 90 1510 16 (3)
Notes Remark
1 REPORTED TO THE GROUND FLOOR
2 TO BE CONFIRMED DURING DETAIL ENGINEERING
3 OSBL CENTRIFUGAL PUMP IS FORESEEN
4 MINIMUM FLOW AT START-UP
6 DISCONTINUOUS FOR CENTRIFUGE WASHING
7 FOR BLANKETING
8 CONSIDER INSULATION FOR HEAT CONSERVATION
9 CONSIDER STEAM TRACING AND INSULATION FOR HEAT CONSERVATION
10 FROM DEDICATED EMERGENCY PUMP OR ESSENTIAL POWER SUPPLY
11 PEAK CONSUMPTION