FPSO FOR SALE OR CHARTER

1997 BLT

DESIGN WIND SPEED: 50 KM/H

AIR RELATIVE HUMIDITY: >80%

AIR TEMPERATURE MIN/MAX: 25.8°C (15/36°C)

SEAWATER SURFACE TEMPERATURE: 28°C

TOPSIDES AVAILABLE AREA: 7,526 M²

CARGO STORAGE EXCL. SLOPS: 96,690 M³ / 608,115 BBL

SLOP TANKS: 3,383 M³ / 21,274 BBL

DIESEL STORAGE: 972 BBL (+19,866 BBL HFO)

CRUDE OIL FEED TEMPERATURE: 70°C

CARGO MAINTAIN TEMPERATURE: 65°C

HEATING DUTY: 44 TO 66°C WITHIN 8 DAYS

OFFLOADING METHOD: TANDEM; HAWSER (80 M)

OFFLOADING RATE: 2 X 2,500 M³/H (4 X 2,500 INSTALLED); 500,000 BPD

MAX OFFLOADING PRESSURE: 135 M/C

WELL COUNT: 5

FWHT AT WELLHEAD: 82°C

ARRIVAL PRESSURE AT TOR: 12.5 BARA

ARRIVAL TEMPERATURE AT TOR: 65–82°C

OIL DENSITY: 31°API

GOR: <10 SCF/BBL

CLOUD POINT: 62°C

POUR POINT: 43°C

WAX CONTENT: 19 WT%

EPC CONTRACTOR: APS / AKER ENGR.

GROSS LIQUIDS: 125,000 BPD

OIL PRODUCTION: 60,000 BPD

PRODUCED WATER MAX: 120,000 BPD

MAX GAS PRODUCED: 0 MMSCFD

GAS TO FLARE: 1 MMSCFD

WATER INJECTION: N/A

CRUDE OIL SEPARATION SUPPLIER: KVAERNER PS

RVP: 10 PSIA (69 KPA)

TVP: MAX 117 KPA AT 70°C

BS&W MAX: 0.3 VOL%

NUMBER OF SEPARATION STAGES: 2

TEST SEPARATOR: N/A

1ST STAGE SEPARATOR DP/OP: 20 / 12.5 BARG/BARA (HP)

1ST STAGE SEPARATOR DT/OT: 125 / 65–95°C

1ST STAGE GAS: 0 MMSCFD

1ST STAGE OIL: 125,000 BPD

1ST STAGE DIMENSIONS: 3,300 X 12,000 MM

INTERMEDIATE STAGE SEPARATOR: N/A (MP)

LAST STAGE SEPARATOR DP/OP: 6 / 1.8 BARG/BARA (LP)

LAST STAGE SEPARATOR DT/OT: 125 / 95°C

LAST STAGE GAS: 1 MMSCFD

LAST STAGE OIL: 72,000 BPD

LAST STAGE DIMENSIONS: 2,500 X 6,000 MM

ELECTROSTATIC DEHYDRATOR OIL: 65,000 BPD (EXCL. 10% WATER)

ELECTROSTATIC DEHYDRATOR DP/OP: 10 / 6 BARG/BARA

ELECTROSTATIC DEHYDRATOR DT/OT: 125 / 95°C

ELECTROSTATIC DEHYDRATOR DIMENSIONS: 3,700 X 8,500 MM

DESALTER: N/A

STABILISER: N/A

CRUDE HEATER: 6,900 KW (1 X 100%)

CRUDE OIL COOLER: 6,375 KW (1 X 100%)

CRUDE OIL TRANSFER PUMPS: 3 X 195 M³/H (3 X 100%)

SAND REMOVAL SYSTEM: N/A

PRODUCED WATER TREATMENT DESIGN CAPACITY: 120,000 BWPD

PRODUCED WATER OIL-IN-WATER: <30 MG/L

PRODUCED WATER PRIMARY SEPARATION: HYDROCYCLONES

WATER DEGASSER: YES

PRODUCED WATER DESTINATION: OVERBOARD

GAS EXPORT PRESSURE AT TOR: N/A

DEHYDRATION SYSTEM: N/A

NGL REMOVAL SYSTEM: N/A

STEAM TYPE: SATURATED STEAM

STEAM SOURCE: 2 STEAM BOILERS

STEAM DESIGN CAPACITY: 2 X 12 T/H

STEAM SUPPLY: 7 BARG / 170°C

HEATING MEDIUM: SATURATED STEAM

COOLING MEDIUM: 30% MEG / 67% WATER / 3% CIT

TOTAL COOLING DUTY: 6,375 KW

COOLING SUPPLY/RETURN: 36°C / —

COOLING DESIGN PRESSURE: 6 BARA

COOLING MEDIUM FLOW: 400 M³/H

COOLING PUMP SPARING: 2 X 50%

COOLING DESIGN T/P: 125°C / 10 BARG

SEAWATER SUPPLY TEMPERATURE: 28°C MAX

SEAWATER TOPSIDES COOLING FLOW: 2 X 500 M³/H

FIREWATER DELUGE: 2 X 1,500 M³/H + 2 X 200 M³/H

FIREWATER PUMP SPARING: 2 X 100% (ONE AT EACH END)

WATER INJECTION SULPHATE REMOVAL: N/A

WATER INJECTION FILTRATION: N/A

WATER INJECTION DEAERATION: N/A

POTABLE WATER STORAGE: 2 TANKS / 241.6 M³ / 1,519 BBL

FRESH WATER STORAGE: 3 TANKS / 772.4 M³ / 4,858 BBL

FRESH WATER GENERATION: 2 X 20 TE/D

SUBSEA CHEMICAL INJECTION: UP TO 4 CHEMICALS, 4 X 10 M³, MAX 207 BARG

START AIR: 2 DUAL-STAGE RECIPROCATING COMPRESSORS

START AIR CAPACITY: 2 X 114 NM³/H

INSTRUMENT AIR: 6 ROTARY SCREW COMPRESSORS

INSTRUMENT AIR CAPACITY: 4 X 250 NM³/H + 1 X 738 NM³/H + 1 X 662 NM³/H

NITROGEN: MEMBRANE SEPARATION

NITROGEN CAPACITY: 2 X 100 SM³/H (2 X 50%)

NACE MR0175 / ISO 15156-3: YES

CRUDE PRODUCTION MATERIAL: CS

PRODUCED WATER MATERIAL: CS

LP SEAWATER MATERIAL: SS316

FLARE HEADERS/TIPS: CS VENT SYSTEM

FLARE KO DRUMS / CLOSED DRAINS: CS

CLOSED DRAIN DRUM: CS

LOCATION: ASIA

STATUS: LAID UP, HULL/SHELL IN GOOD CONDITION

WOG / SUBJECT TO AVAILABILITY

FURTHER DETAILS TO NAMED INTEREST ONLY