2 refineries available in Europe
one for dismantling;
Refining capacity: 5.5 million tonnes per
year.
Product output:
Ultra-Low Sulphur Diesel & Bio-Diesel
Kerosene & Gas Oil
Petrochemical Feedstock’s
Unit History - There have been upgrades spent on this
refinery over the past number of years including £23M
increasing the size of vessels and output volumes and a
nitro system to maintain certain parts of the plant.
40
million sterling
Must be dismantled - the buyer can rebuild anywhere worldwide - we have a company that has already inspected the refinery and is capable of doing the job. To enquire further about this refinery for sale please contact us here
T he
other including 70
hectares of land upon which it stands with a pipeline to
port - Refinery and pipe line are Nitrogen purged.
Tank farm including 54 tanks at
capacity 486000 m3.
425 million sterling To enquire further about this refinery for sale please contact us here
100,000 BPDD Oil Refinery & Aromatics Processing Plant.
- SOLD
-
100,000 BPD OIL REFINERY FOR SALE; THIS OIL REFINERY AND AROMATICS PROCESSING PLANT IS FULLY OPERATIONAL AND ACTUALLY PRODUCING 100,000 BARRELS PER DAY. THE PLANT IS FOR SALE AS A COMPLETE PLANT AND THE SELLER DOES NOT WANT TO SELL COMPONENTS OR PARTS; THE BUYER WILL HAVE TO DISMANTLE THE COMPLETE REFINERY DESCRIBED BELOW AT BUYER'S EXPENSE AND PAY FOR THE TRANSPORTATION FROM ACTUAL SITE TO BUYER'S SITE. THE BUYER WILL HAVE TO DISMANTLE THE EXISTING PLANT ACCORDING TO ENVIRONMENTAL LAWS OF THE COUNTRY WHERE THE REFINERY IS LOCATED.
DETAILS PERTAINING TO THE REFINERY AND AROMATICS PROCESS PLANT ARE
OBTAINED FROM SOURCES DEEMED RELIABLE; HOWEVER WE CANNOT GUARANTEE THEIR
COMPLETE ACCURACY TO OUR HIGHER STANDARD AT THIS TIME. WE WILL HELP
BUYER VERIFY THE ACCURACY OF THE INFORMATION AND PHOTO RECORD ABOUT THE ITEMS TO
BE PURCHASED.
PRODUCTION CAPACITIES OF THE PLANT.
- ATMOSPHERIC CRUDE DISTILLATION..................100,000 BPD
- VACUUM CRUDE DISTILLATION.................... 30,000 BPD
- C5 SPLITTER...............................* BPD
- VISBREAKER................................8,700 BPD
- THERMAL CATALYTIC CRACKING.....................20,000 BPD
- CATALYTIC REFORMING
- REFORMER #1 (GAS PLANT EXPANSION 1986)...............13,000 BPD
- CATALYTIC DESULPHURIZATION......................15,000 BPD
- C3 AND C4 SPLITTER..........................* BPD
- MEROX TREATMENT...........................12,000 BPD
- ASPHALT BLENDING...........................4,000 BPD
- SULPHUR RECOVERY................................70 TPD
- FEED PREPARATION UNIT FOR REFORMERS................28,000 BPD
- ALKYLATION'S UNIT...........................3,800 BPD
3- AROMATICS PROCESS PLANT
- BENZENE - TOLUENE - XYLENES SUPER FRACTIONATION
- TOLUENE DISPROPORTIONATION UNIT
- UDEX EXTRACTION UNIT
- L.P. REFORMER # 2
4- OTHER ASSOCIATED PLANT SYSTEMS
- CYCLO HEXANE
- WASTE WATER TREATMENT PLANT
- STORAGE TANKS
- PACKAGE BOILERS
- ANCILLARY EQUIPMENT
-GENERATORS / TRANSFORMERS
- SPARE PARTS
- WORKSHOP EQUIPMENTS
- MOBILE PLANT
2) THE 100,000 BPD OIL REFINERY DESCRIPTION
A) ATMOSPHERIC CRUDE DISTILLATION UNIT (100,000 BPD) REVAMPED IN 1981.
- FRACTIONING SECTION
- TWO TRAINS OF FEED / EFFLUENT EXCHANGERS
- TWO DESALTERS, FOUR FEED / EFFLUENT EXCHANGERS
- TWO EFFLUENT COOLERS
- TWO PREHEATING FURNACES
- ATMOSPHERIC TOWER DISTILLATION COLUMN 6.1m DIA. X 40.2m HIGH
- OVERHEAD COOLER
- REFLUX COOLER AND DRUM
- KEROSENE , LIGHT AND HEAVY GAS OIL STRIPERS
- KEROSENE LIGHT GAS OIL EFFLUENT EXCHANGERS AND COOLERS
- RESIDUE AND HEAVY GAS OIL COOLERS
- STABILIZATION AND GAS SECTION
- TWO FEED / EFFLUENT EXCHANGERS
- STABILIZER TOWER 2.9 METERS DIAMETER BY 42.7 METERS HIGH
- TWO NAPHTHA COOLERS
- OVERHEAD CONDENSERS AND DRUM LPG COOLER
- TWO STAGES RECIPROCATING COMPRESSORS AND FIVE DRUMS
B) VACUUM CRUDE DISTILLATION UNIT (30,000 BPD) INSTALLED IN 1989
- NEW VACUUM CRUDE DISTILLATION
- NEW VACUUM FLASH TOWER
- VACUUM TOWER 4.4m DIA. X 21.2m HIGH
- FOUR OVERHEAD CONDENSERS AND DRUM
- TWO OVERHEAD REFLUX AIR COOLERS
- SIX EXCHANGERS
C) C5 SPLITTER
- FRACTIONATOR TOWER OVERHEAD COOLERS AND DRUMS
- SURGE TANK
- FEED / EFFLUENT EXCHANGER
- BOTTOM REBOILERS ISOPENTANE AND NORMAL PENTANE COOLERS
D) VISBREAKER (8,700 BPD) INSTALLED IN 1986
- ONE TRAIN OF FEED
- VACUUM AND FRACTIONATOR BOTTOM EXCHANGERS
- THREE STEAM GENERATORS
- PRE HEATING FURNACES
- VACUUM TOWER OVERHEAD CONDENSERS
- DRUM BOTTOM COOLER
- FRACTIONATING TOWER OVERHEAD AIR COOLER DRUM
- GAS OIL STRIPPER AND COOLER
- TWO HEAVY VACUUM GAS OIL
- TWO LIGHT VACUUM GAS OIL COOLERS
- DECOKING DRUM AND DRY GAS TANK
- TWO AIR COMPRESSOR DRYERS AND ACCUMULATORS
E) THERMAL CATALYTIC CRACKING UNIT (20,000 BPD)
1 - FEED PREPARATION SECTION REVAMPED IN 1985
- ONE TRAIN RESIDUE FEED / EFFLUENT EXCHANGERS
- ONE TRAIN HEAVY GAS OIL FEED / EFFLUENT EXCHANGER
- RESIDUE AND HEAVY GAS OIL HEATING FURNACE
- TAR SEPARATION 3.3m DIA. X 6.6m HIGH
- VACUUM TOWER 5.4m DIA. X 24.7m HIGH , OVERHEAD CONDENSERS
- REFLUX AND LIGHT VACUUM GAS OIL COOLERS
- VACUUM OVER FLASH LIGHT AND HEAVY VACUUM GAS OIL DRUMS
- VACUUM FILTERS BOTTOM EXCHANGER AND COOLERS
2 - CATALYTIC SECTION REVAMPED IN 1989
- REACTOR 4.9m DIA. X 18m HIGH
- SEPARATOR SURGE DRUM 3.0m DIA. X 13.5m HIGH
- CATALYST HOT STORAGE TANK 9.9m DIA. X 13.8m HIGH
- CATALYST REGENERATION
- AIR COMBUSTION AIR LIFT FURNACES
- CO BOILER (1983)
3 - FRACTIONING SECTION
- SYNTHETIC TOWER 4m DIA. X 20m HIGH WITH OVERHEAD CONDENSERS
- DRUM AIR COOLERS
- SYNTHETIC TOWER BOTTOM STEAM GENERATOR AND COOLER
- FINE SEPARATORS REFLUX EXCHANGER LEAN OIL STRIPPERS
4 - GAS SECTION
- TWO STAGES RECIPROCATING COMPRESSOR , TURBINE AND CONDENSER
- STAGE 1 AND 2 KO DRUM AIR COOLERS , COOLERS AND ACCUMULATORS
- PRE-ABSORBER TOWER 2.4m DIA. X 17.7m HIGH
- ABSORBER TOWER 0.95m DIA. X 19.5 HIGH AIR COOLERS AND COOLERS
- DE-ETHANIZER TOWER 1.7m DIA. X 20.4m HIGH
- OVERHEAD CONDENSER DRUM SEPARATOR AND BOTTOM REBOILER
- DEBUTANIZER TOWER 1.5m DIA. X 29.7m HIGH
- OVERHEAD CONDENSER AND DRUM DEBUTANIZER BOTTOM REBOILER
- EXCHANGER AND COOLERS
- FRACTIONATOR TOWER 1.1m DIA. X 21.4m HIGH
- OVERHEAD CONDENSER AND DRUM FRACTIONATOR
- BOTTOM REBOILER COOLERS AND REFLUX COOLERS
5 - ETHYLATE SECTION
- FRACTION TOWER 1.1m DIA. X 17.4m HIGH
- OVERHEAD CONDENSER AND DRUM BOTTOM REBOILER
- WATER SEPARATOR
F) CATALYTIC REFORMER (13,000 BPD)
- PREHEATING SECTION
- ONE TRAIN REACTOR FEED / EFFLUENT EXCHANGERS
- PRE-HEATING FURNACE
- REACTOR 1.6m DIA. X 9.8 HIGH
- REACTOR EFFLUENT COOLERS AND AIR COOLERS
- HIGH TEMPERATURE SEPARATOR
- STABILIZER TOWER 2.8m DIA. X 37.6m HIGH
- FEED BOTTOM EXCHANGER, OVERHEAD AIR COOLERS, COOLER AND DRUM
- STABILIZER BOTTOM REBOILER FURNACE
- ABSORBER TOWER 1.8m DIA. X 24.9m HIGH
- OVERHEAD CONDENSER AND DRUM
G) REFORMER SECTION WITH GAS PLANT REVAMPED IN 1986
- ONE TRAIN REACTOR FEED / EFFLUENT EXCHANGERS
- REACTOR FEED PREHEATING FURNACES (3 OFF) AND REBOILER
- THREE REACTORS, EACH 3.8m X 5.3m HIGH
- EFFLUENT COOLERS
- HIGH PRESSURE SEPARATOR
- STABILIZER TOWER 1.8m DIA. X 20.2m HIGH FEED AND BOTTOM EXCHANGER
- BOTTOM REBOILER AND COOLER AND DRUMS
H) MEROX TREATMENT INSTALLED IN 1982
1 - KEROSENE MEROX UNIT (12,000 BPD)
- ELECTRO PRECIPITATOR
- TWO MEROX REACTORS CAUSTIC SETTLER
- WATER WASH , SALT AND CLAY FILTERS , KO AND SEAL DRUMS
- TANKS FOR MEROX CATALYST MIXING ACELIC ACID ANTIOXYDANT SOLUTION
- KERO FEED HEATER AND COOLER
- TWO AIR COMPRESSORS
- AIR ACCUMULATOR , AIR COOLERS AND MIXERS
2 - LPG MEROX AND WASHING UNITS
- CRUDE FLOW
- EXTRACTOR TOWER 1.4m DIA. X 25.7m HIGH
- CAUSTIC SETTLER AND SAND FILTER DRUM
- NAPHTHA WASHING SEPARATOR
3 - REFORMER FLOW
- CONTACT TOWER 0.85m DIA. X 9.0 m HIGH
- CAUSTIC AND WATER SETTLING DRUMS
4 - TCC FLOW
- EXTRACTOR TOWER 1.39m DIA. X 15.1m HIGH
- OVERHEAD SEPARATOR DRUM AND FILTER
- CAUSTIC ACCUMULATOR
- OXIDIZER DRUM
- DESULPHUR SEPARATOR
- EXHAUSTED AIR SEPARATOR
- AIR ACCUMULATOR AND AIR COMPRESSOR
H) CATALYTIC DESULPHURRISATION UNIT (15,000 BPD) REVAMPED IN 1986
- DEREACTOR TOWER 1.9m DIA. X 15.8m HIGH
- TWO REACTORS 2.1m DIA. X 9m AND 10.7m HIGH
- STRIPPER TOWER 1.8m DIA. X 24.2m HIGH
- HIGH TEMPERATURE AND LOW PRESSURE SEPARATOR
- STRIPPER AND OVERHEAD DRUM
- ONE FEED / EFFLUENT EXCHANGER
- ONE FEED / STRIPPER BOTTOM REACTOR EFFLUENT EXCHANGER
- HYDROGEN RECIRCULATION / REACTOR EFFLUENT EXCHANGER
-HIGH PRESSURE OVERHEAD AND LOW PRESSURE BOTTOM COOLERS
- STEAM GENERATOR STRIPPERS OVERHEAD
- BOTTOM CONDENSERS AND COOLERS
J) ASPHALT BLENDING (4,000 BPD)
- FIVE STEAM CONDENSATE SEPARATORS
- TWO FLASH DRUMS
- THREE ASPHALT HEATERS
- INSTRUMENT AIR ACCUMULATOR
K) SULPHUR RECOVERY UNIT (70 TPD) INSTALLED IN 1980
1 - AMINE SECTION
- GAS ABSORBER TOWER 2.4m DIA. X 22.4m HIGH
- AMINE REGENERATION TOWER 1.8m DIA. X 22.3m HIGH
- TWO LPG ABSORBERS 0.93m DIA. X 15m HIGH
- TWO FEED SEPARATORS OVERHEAD DRUM
- STEAM CONDENSATE CONTROL AND SEPARATE DRUMS
- FRESH AND DILUTED AMINE TANKS AND FILTERS
- TWO OVERHEAD AIR COOLERS FEED BOTTOM EXCHANGERS
- BOTTOM REBOILERS
2 - SULPHUR SECTION
- AMINE SEPARATOR 3 STAGES CONVERTER STEAM CONDENSATE SEPARATORS
- BLOW DOWN DRUM
- LIQUID GAS SEPARATOR AND AMINE FILTERS
- LIQUID SULPHUR TANK AND HEATERS
- FOUR STAGES CONDENSERS
- THREE STAGE FEED CONVERTER HEATERS FOR STEAM CONDENSATE
- AIR CONDENSER
- REACTION FURNACE
- STEAM BOILER
- FUME OXIDATOR
- TANK
- AIR BLOWERS
L) ALKYLATION UNIT (3,800 BPD)
- PREPARATION SECTION
- FEED PREHEATER
- DEPROPANISER TOWER 1m DIA. X 20.1m HIGH
- OVERHEAD CONDENSERS AND DRUMS
- STEAM REBOILER
- DEISOBUTANIZER TOWER 1.6m DIA. X 20.1m HIGH
- OVERHEAD CONDENSERS AND DRUMS
- STEAM REBOILER AND COOLER
M) FEED PREPARATION UNIT FOR REFORMERS (28,000 BPD)
1 - NAPHTHA SPLITTER SECTION
- NAPHTHA SPLITTER TOWER 3.3m DIA X 33.9m HIGH
- OVERHEAD AIR COOLERS , DRUM AND COOLER
- FEED BOTTOM AND OVERHEAD EXCHANGERS
- TWO BOTTOM AIR COOLERS
- BOTTOM REBOILER FURNACE
2 - DEPENTANISER SECTION
- DEPENTANIZER SPLITTER TOWER 2.2m DIA. X 28m HIGH
- OVERHEAD COOLERS,DRUM AND COOLER
- TWO BOTTOM AIR COOLERS
- DRY GAS TANK
- BOTTOM REBOILER FURNACE
3 - REFORMATE SPLITTER SECTION
- REFORMATE SPLITTER TOWER 2.6m DIA. X 32.6m HIGH
- OVERHEAD COOLER, DRUMS AND SEVEN COOLERS
- TWO BOTTOM AIR COOLERS
- BOTTOM REBOILER FURNACE
4 - ACID SECTION (HF)
- FEED DRYERS
- REGENERATION HEATER AND CONDENSER
- ACID SETTLING TANK , STORAGE DRUMS AND COOLER
- RE-RUN COLUMN VAPORIZER , HEATER AND RE-CYCLE COOLER
- MAIN FRACTION TOWER 3.0m DIA. X 51.1m HIGH
- EXCHANGERS STRIPPER CONDENSERS AND DRUMS
- FRACTION REBOILER
- PROPANE STRIPPER
- DEFLOURINATORS
- CAUSTIC TREATERS AND CONDENSERS
- ALKYLATE COOLER
- ACID RELIEF NEUTRALIZER
3 - AROMATICS PROCESS PLANT
A)TOLUENE DISPROPORTIONATION UNIT (TDP)
- FEED DRYERS
- THREE TRAINS OF FEED EFFLUENT EXCHANGERS
- HEATING FURNACE 4.7 MMK CAL./HOUR
- REACTOR 2.3m DIA. X 19.4m HIGH
- EFFLUENT CONDENSER, SEPARATOR DRUM AND COOLER
- STABILIZING TOWER 1.1m DIA. X 19.4m HIGH
- STABILIZER OVERHEAD CONDENSER AND RECEIVER
- STABILIZER REBOILER
- RECYCLE GAS COMPRESSOR (2 OFF)
- GAS RECYCLE GAS DRYERS
B) BENZENE - TOLUENE - XYLENES SUPERFRACTION UNIT (BTX)
- FEED EXCHANGERS
- BENZENE TOWERS (12 OFF) 3.4 TO 3.8m X 57.9m HIGH
- TOLUENE TOWERS (13 OFF) 3.3 TO 3.5m X 57.6m HIGH
- BENZENE HEATING FURNACE 10.0 MMK CAL./HOUR
- TOLUENE HEATING FURNACE 15.6 MMK CAL./HOUR
- OX-XYLENE TOWER 1.5m DIA. X 37.2m HIGH
- BENZENE OVERHEAD RECEIVERS, CONDENSERS AND COOLERS
- TOLUENE OVERHEAD RECEIVERS, CONDENSERS AND COOLERS
- XYLENES COOLERS
- AROMATICS TOWERS 1.5m DIA. X 37.2m HIGH
- REBOILERS (2 OFF) CONDENSERS AND RECEIVERS
C) UDEX EXTRACTION UNIT
- FEED EXCHANGERS
- COOLERS , CONDENSERS AND REBOILERS
- EXTRACTOR TOWER 3.4m DIA. X 31m HIGH
- STRIPPER COLUMN 3.2m DIA. X 46.5m HIGH
- TOWER 2.6m DIA. X 9,8m HIGH
D) CYCLOHEXANE UNIT
- PRIMARY REACTOR 1.8m DIA. X 13.7m HIGH
- FINISHING REACTOR 1.0m DIA. X 18.0m HIGH
- STABILIZER TOWER 1.0m DIA. X 18.0m HIGH
- COOLERS , CONDENSERS AND EXCHANGERS
- FEED GAS AND H2 BOOSTER COMPRESSORS
- DRUMS AND SEPARATORS
E) L. P. REFORMER (REFORMER # 2) (REFORMER SECTION)
- FEDD EXCHANGERS
- THREE PREHEATING FURNACES
- THREE REACTORS 3.8m DIA.
- STRIPPER COLUMN 2m DIA. X 31.0m HIGH
- DEBUTANISER TOWER 1.7m DIA. X 22.6m HIGH
- RECYCLE GAS COMPRESSOR , AIR COOLERS ,CONDENSERS AND RECEIVERS
F) DESULPHURISATION SECTION (HYDROTREATER)
- FEED EXCHANGERS
- CHARGE HEATER AND REACTOR
- STABILIZING COLUMN
- MAKE UP AND RECYCLE GAS COMPRESOR
- CONDENSERS AND RECEIVERS
4) OTHER ACCESSORY PLANT SYSTEMS
A) AROMATICS WASTE WATER TREATMENT PLANT ( 60 CUBIC METERS /HOUR)
B) BOILER FEED WATER PLANT
C) DEMINERALISATION UNIT ( 200 CUBIC METERS /HOUR)
D) STORAGE TANKS
E) AROMATICS PRODUCT STORAGE TANKS (FIXED ROOF); VARIOUS SIZES FROM 760
CUBIC METERS TO 4000 CUBIC METERS; PENTANE AND LPG SPHERES
F) ANCILLARY EQUIPMENT
G) GENERATORS , TRANSFORMERS. SPARE PARTS , WORK SHOP EQUIPMENTS
H) COMPRESSORS AND MOBILE PLANT
I) PACKAGE BOILERS
TERMS & CONDITIONS:
- 15% IN ESCROW WITH THE OFFER PLUS TRAVELLING EXPENSES OF BROKER PAID
($40,000 USD APPROX.)
- BALANCE AT ACCEPTANCE
- DISMANTLING AND TRANSPORTATION OF EQUIPMENT AT THE BUYER'S EXPENSE.
- DISMANTLING AND TRANSPORTATION TO BE DONE ACCORDING TO ENVIRONMENTAL
LAWS OF THE COUNTRY WHERE THE REFINERY IS IN OPERATION.
- THERE ARE NO GUARANTEES ON ANY OF THE EQUIPMENT LISTED.
- DETAILS PERTAINING TO THE ABOVE REFINERY AND AROMATICS PROCESS
PLANT ARE OBTAINED FROM SOURCES DEEMED RELIABLE; HOWEVER WE CANNOT GUARANTEE
THEIR ACCURACY .
- WE WILL HELP BUYER VERIFY THE ACCURACY OF THE INFORMATION ABOUT THE ITEMS TO BE PURCHASED.
PRICE : 44,500,000.;USD AS IS WHERE IS.
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1 PURCHASE 44,500,000.00 USD (PLUS ANY TAXES REQUIRED IN BUYER'S COUNTRY);
2 MARK, TAG, SUPERVISE LOAD OUT AND SHIP OVER ABOUT 1 TO 2 YEARS $50,000,000.
3 PREPARE SITE, SET UP AND MAKE INITIAL TEST/TRAINING RUN $250,000,000. TO $300,000,000.
4 CRUDE AND PRODUCT TANK FARM AND CRUDE OIL STOCK OPERATING CAPITAL TO
HOLD SUPPLY OF ABOUT 3,000,000 BBL, 30 TO 45 DAYS SUPPLY $125,000,000.
5 TOTAL IS $452,000,000. TO $502,000,000.
6 A REFINERY LIKE THIS WITHOUT LAND, SHIPPING AND ACCESSORY EQUIPMENT
COSTS $1.6 BILLION NEW, WOULD TAKE ABOUT 5 YEARS TO GET IN OPERATION AND THIS WILL HAVE
A USEFUL LIFE OF ABOUT 20 YEARS WITH NORMAL MAINTENANCE.
SOLD
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This one is sold, however we have one which could be upgraded to 40,000 bbls/day and one of 30,000 barrels per day completely rebuilt with warranty with new (DCS) and ready to ship accordingly to proposal.
Please contact us here
If you let us know your requirements we will try to match. |
