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Ref.-No.:

ProOil-276

Presented by: LOHRMANN RBD (Refinery Business Division)

100,000 bpd Refurbished Oil RefineryFOR SALE AND RELOCATION

REFURBISHED OIL REFINERY FOR SALE AND RELOCATION Ref.-No.: ProOil-276

1. Process Units

CapacityDescription barrels per day Licensor Designer/Constructor Year

CDU Atmospheric Distillation Unit 100,000 Socony Mobil Oil FosterWheeler 1962

VDU Vacuum Distillation Unit 25,000 NEW to build

NCHD Naphta Hydrotreater 24,000 Socony Mobil Oil Foster Wheeler 1962NCHD Naphta Hydrotreater 24,000 Socony Mobil Oil Foster Wheeler 1962

Platformer (Platinum Reformer) 14,000 Socony Mobil Oil Foster Wheeler 1962

KCHD Kerosene Hydrotreater 12,000 Socony Mobil Oil Foster Wheeler 1962

LPG Treatment 4,000 Socony Mobil Oil Lummus 1980

AMU Amine Treating Unit 653 321 ft³/hr Snamprogetti 1995

SRU Sulphur Recovery Unit 44,100 lbs/d Snamprogetti 1995

SSFU Solid Sulphur Forming Unit (Flaker) 44,100 lbs/d 1995

FCCU Fluid catalytic cracker 13,000 NEW to build


2. History

Brief summary of the equipment concerned, their capacities and brief engineering history up to shut down in 2004:

2.1 Process Unit’s History

1962 Commissioning

1981 Commissioned De-bottlenecked to 100,000 BPSD1981 Commissioned De-bottlenecked to 100,000 BPSD- added second parallel pre heat-exchanger train- doubled overhead cooling capacity, and- installed booster feed pump

Installed new desalter

Modified tower internals removed two trays and replaced two others with packedsection and bubble cap tray.

1992 CDU ENCON Project Phase-1- installed four pre heat-exchangers (two new and two idle)- modified tower internals, and- raised gasoil draw

1994 CDU ENCON Project Phase-II- installed six new pre heat-exchangers


1997 CDU Tower Modifications- installed new sieve trays at stripping section- installed new steam distributors at stripping section- installed new VEP type gravity liquid distributor- removed random packing and- removed bubble cap tray no 6 installed new low pressure drop de-entrainment tray- installed new HGO draw nozzles

2.2 Key Unit’s History and Capacities

Crude Distillation Unit

HISTORYHISTORY

1962 Commissioned at 68.500 BPSD capacity

1969 Debottlenecked to 100.000 BPSD capacity- added second parallel pre heat-exchanger train- doubled overhead cooling capacity, and- installed booster feed pump

Installed new desalter

1975 Modified tower internals, removed two trays and replaced two others with packed sectionand bubble cap tray.

1992 CDU ENCON Project Phase 1- installed four pre heat-exchangers (two new and two idle)- modified tower internals, and- raised gasoil draw


1994 CDU ENCON Project Phase 2- installed six new pre heat-exchangers

1997 CDU Tower Modifications- installed new sieve trays at stripping section- installed new steam distributors at stripping section- installed new VEP type gravity liquid distributor- removed random packing and- removed bubble cap tray no. 6. Installed new low pressure drop de-entrainment tray,- installed new HGO draw nozzles

Naphtha Catalytic Hydrodesulphurisation Unit NCHD

HISTORY

1962 Commissioned at 19,000 BPSD capacity.

1969 Commissioned and De-bottlenecked to 21,700 BPSD- added pre heat-exchangers

1998 De-bottlenecking to 24,000 BPSD- added pre heat-exchangers

UNIT CAPACITY 24,000 BPSD 158.9 m3/hr

CATALYST Akzo KJ-752-3Q 7,560 kgCriterion C-448 TL + 7,780 kgTotal 15,340 kg


Platinum Reforming Unit PtR

HISTORY

1962 Commissioned at 8000 BPSD capacity,

1970 Installed smaller capacity spare recycle gas compressor

1991 Expanded to 14,000 BPSDre-trayed stabilizer toweradded five new heat-exchangers, andadded fourth reactor (radial flow)added fourth reactor (radial flow)

1996 New Recycle gas compressor installed

UNIT CAPACITY 14,000 BPSD 92.7 m3/hrsix -month cycle @ 96 RON clear severity

CATALYST U O P R–62 P t / R h :

in spherical reactor # 1 (D-300) 6,000 kgin spherical reactor # 2 (D-301) 6,617 kgin spherical reactor # 3 (D-302) 6,645 kgin new radial reactor # 4 (D-351) + 29,956 kg

49,218 kg


Kerosene Catalytic Hydrodesulphurisation Unit KCHD

HISTORY

1962 Commissioned at 8,000 BPSD capacity

1969 Expanded to 12,000 BPSD kerosene

1988 After Diesel specification reduced to 0.7 %wt S. Gasoil de-sulphurisation in block operationat 10,000 BPSD maximum capacity

1997 Dense loading of reactor performed. New distribution tray installed.1997 Dense loading of reactor performed. New distribution tray installed.

UNIT CAPACITY 12,000 BPSD Kerosene: 79.5 m3/hr10,000 BPSD Gas oil: 66.25 m3/hr

Liquefied Petroleum Gas Unit LPG

HISTORY

1980`s Commissioned at 2,800 BPSD capacity

Designed for mild desulphurisation of kerosene

Expanded to 4,000 BPSD along with PtR

UNIT CAPACITY 4,000 BPSD 26.5 m3/hr


Amine Treating Unit ARU

HISTORY

1995 Commissioned to treat 18,500 m3/hr fuel gas containing 26 kmoles/hr H2S.Specified to meet down to 0.4 – 5.0 %vol H2S in fuel gas (- 2 tons/day)

UNIT CAPACITY 18,500 M3/HR Fuel Gas

Sulphur Recovery Unit SRU

HISTORY

1995 Commissioned to recover 20 tons/day sulphur- Three- stage Claus plant, single train: 6.6 to 1 turn-down ratio.Incinerator but no tail gas unit.

- Sulphur Recovery is 97% at SOR, 96% at EOR- SO2 emission < 70 kg/hr

UNIT CAPACITY 20 tons/day

Solid Sulphur Forming Unit Flaker

HISTORY

1995 Commissioned to process 30 tons/day liquid sulphur solid sulphur flakes


Vacuum Distilation Unit VDU (Added)

HISTORY

XXXXUNIT CAPACITY

Fluid Catalytic Cracker FCCU (Added)

HISTORY

XXXXUNIT CAPACITY 13,000 BPSD Heavy Gasoil: 86,7 m3/hr

Feed ConCarbon wt%


ADDITIONAL INFORMATION ABOUT PROCESSING UNITS REVELANT UDGRADES

1. ATMOSPHERIC CRUDE DISTILLATION UNIT

a) Capacity: 100 ,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Foster Wheelerc) Year of relevant upgrade: 1992 ENCON Project Phase 1

1994 ENCON Project Phase 21997 Atmospheric Tower Modification1997 Atmospheric Tower Modification

2. NAPHTHA CATALYTICAL HYDRODESULFURIZATION UNIT

a) Capacity: 24,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Foster Wheelerc) Year of relevant upgrade: 1969 De-bottlenecked to 21,700 BPSD

1998 De-bottlenecked to 24,000 BPSD

3. PLATINUM REFORMING UNIT

a) Capacity: 14,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Foster Wheelerc) Year of relevant upgrade: 1991 De-bottlenecked to 14,000 BPSD

1996 New recycle gas compressor was taken into service.


4. KEROSENE CATALYTICAL HYDRODESULFURIZATION UNIT

a) Capacity: 12,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Foster Wheelerc) Year of relevant upgrade: 1969 Expanded to 12,000 BPSD Kerosene

1988 Modified for gasoil desulphurisation at 10,000 BPSD1999 De-bottlenecked to 12 TBD with gas oil

5. LIQUEFIED PETROLEUM GAS UNIT

a) Capacity: 4,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Lummusb) Whose technology: Socony Mobil Oil, installed by Lummusd) Year of relevant upgrade: 1980`s Designed for mild de-sulfurization of

kerosene to 4,000 BPSD along with PtR

6. AMINE TREATMENT AND RECOVERY UNIT

a) Capacity: 18500 m3/h fuel gasb) Age: 13 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.

7. SULFUR RECOVERY UNIT

a) Capacity: 20 ton/day of liquid sulfurb) Age: 13 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.


8. SOLID SULFUR FORMING UNIT ( FLAKER )

a) Capacity: 30 ton/day of sulfur flakesb) Age: 9 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.

9. VACUUM DISTILATION UNIT

a) Capacity: 4,000 BPSDb) Whose technology: Socony Mobil Oil, installed by Lummusd) Year of relevant upgrade: 1980`s Designed for mild de-sulfurization ofd) Year of relevant upgrade: 1980`s Designed for mild de-sulfurization of

kerosene to 4,000 BPSD along with PtR

6. AMINE TREATMENT AND RECOVERY UNIT

a) Capacity: 18500 m3/h fuel gasb) Age: 13 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.

7. SULFUR RECOVERY UNIT

a) Capacity: 20 ton/day of liquid sulfurb) Age: 13 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.


8. SOLID SULFUR FORMING UNIT ( FLAKER )

a) Capacity: 30 ton/day of sulfur flakesb) Age: 9 years oldc) Whose technology: Snamprogettid) Year of recent upgrades: None.

OTHER PROCESS UNITS CAN BE ADDED DEPENDANT ON CUSTOMERS PRODUCT REQUIREMENTS(i.e. ANOTHER FCCU OR VACUUM DISTILLATION UNIT)


CUTS

ASTM endpoint °C Light products

Isa naphtha 71swing stream # 1 82 minimum gasolineswing stream # 2 104h s e naphtha 154

3. Feedstock & Products

swing stream # 3 160 maximum gasolineswing stream # 4 171swing stream # 5 182

kerosene 271 jet A – 1kerosene 310 product kerosene

swing stream # 6 310 dieselgas oil 388swing stream # 7 396swing stream # 8 400 – 410residuum 410


Crude Oil Throughput History Between 1998 – 2002 (1 Q)

x 1000 Metric Tons per Year

Year: 1998 1999 2000 2001 2002-(Q1)

Crude Oil Input Gravity API 33.2 33.2 32.8 31.9 32.5

Indigenous Mix 508.0 522.0 536.8 325.6 96.8Forozan 78.6 76.1 0.0 70.8 0.0Kerkuk 0.0 409.7 1,050.9 404.1 6.7E. Sider 78.7 0.0 75.0 5.6 15.1Iranian Heavy 223.2 252.3 94.0 1.4 0.0Urals 325.6 1,478.3 222.8 674.8 0.6Syrian Light 297.3 105.7 404.9 526.2 113.1Saharan 77.7 62.1 19.2 76.6 21.9Saharan 77.7 62.1 19.2 76.6 21.9Syrian Blend 760.4 208.0 363.2 864,8 283.3Iran. Light 51.6 9.4 0.0 0.0 101.6Basra Light 138.4 70.9 84.4 158.0 0.0Siberian Light 66.6 261.6 97.4 3.7 29.7Didon 0.0 44.0 0.0 0.0 0.0Arabian Light 117.8 0.0 0.0 0.0 0.0Arabian Heavy 102.1 0.0 0.0 0.0 0.0Arabian Medium 79.4 0.0 0.0 0.0 0.0Maya 77.4 0.0 0.0 0.0 0.0Ras Gharip 148.4 74.4 0.0 0.0 0.0Brent 3.3 0.0 0.0 0.0 0.0Tengiz 357.0 149.5 0.0 0.0 0.0Zueitina 0.0 0.0 0.0 36.2 7.3Total 3,486.3 3,724.1 2,948.7 3,100.9 676.0

Import H.F.O 0.0 0.0 11.6 0.0 0.0Additives 0.5 0.5 0.3 0.4 0.1

Total Input 3,486.8 3,724.5 2,960.6 3,101.2 676.1


Production History Between 1998 – 2002 (1 Q)

Refinery Production 1998 1999 2000 2001 2002-(1 Q)

LPG 83.1 76.1 73.7 68.5 15.8

Premium Gasoline 150.8 168.5 116.9 135.3 28.9

Regular GasolineRegular Gasoline 299.1 317.7 217.1 164.8 42.0

Unleaded Gasoline 58.9 47.0 78.3 127.2 36.0

Jet A-1 0.0 0.0 0.0 0.0 0.0

Kerosene 8.0 7.5 6.9 3.2 0.9

All – Purpose Diesel 1,101.3 1,330.7 1,019.1 997.6 204.4

Home Heating Oil 117.7 150.4 157.8 109.6 32.4

No. 6 Fuel Oil 1,550.0 1,499.5 1,190.2 1,372.1 283.8

Flaked Sulphure 3.0 1.9 2.0 2.9 0.8

Naphta 0.0 0.0 0.0 28.0 3.8

Total Saleable 3,371.8 3,599.2 2,862.0 3,009.1 648.9

Unfinished Product -5.3 10.4 -8.6 -19.4 1.5


4. Pictures


Thank you !

Sonnenberger Strasse 16

65193 Wiesbaden, Germany

Tel. +49 611 701888

Fax +49 611 701895

www.lohrmann.com

[email protected]

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