100,000 bpd Refurbished Oil Refinery FOR SALE AND RELOCATION

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1 Ref.-No.: ProOil ,000 bpd Refurbished Oil Refinery FOR SALE AND RELOCATION Presented by: LOHRMANN RBD (Refinery Business Division)

2 1. Process Units Capacity Description 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 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 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

3 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 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 packed section and bubble cap tray 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

4 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 HISTORY 1962 Commissioned at BPSD capacity 1969 Debottlenecked to BPSD capacity - added second parallel pre heat-exchanger train - doubled overhead cooling capacity, and - installed booster feed pump Installed new desalter REFURBISHED OIL REFINERY FOR SALE AND RELOCATION Ref.-No.: ProOil Modified tower internals, removed two trays and replaced two others with packed section and bubble cap tray CDU ENCON Project Phase 1 - installed four pre heat-exchangers (two new and two idle) - modified tower internals, and - raised gasoil draw

5 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 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 m3/hr CATALYST Akzo KJ-752-3Q 7,560 kg Criterion C-448 TL + 7,780 kg Total 15,340 kg

6 Platinum Reforming Unit PtR HISTORY 1962 Commissioned at 8000 BPSD capacity, 1970 Installed smaller capacity spare recycle gas compressor 1991 Expanded to 14,000 BPSD re-trayed stabilizer tower added five new heat-exchangers, and added fourth reactor (radial flow) 1996 New Recycle gas compressor installed UNIT CAPACITY 14,000 BPSD 92.7 m3/hr six -month 96 RON clear severity CATALYST U O P R 62 P t / R h : in spherical reactor # 1 (D-300) in spherical reactor # 2 (D-301) in spherical reactor # 3 (D-302) in new radial reactor # 4 (D-351) 6,000 kg 6,617 kg 6,645 kg + 29,956 kg 49,218 kg

7 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 operation at 10,000 BPSD maximum capacity 1997 Dense loading of reactor performed. New distribution tray installed. UNIT CAPACITY 12,000 BPSD Kerosene: 79.5 m3/hr 10,000 BPSD Gas oil: 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

8 Amine Treating Unit ARU HISTORY 1995 Commissioned to treat 18,500 m3/hr fuel gas containing 26 kmoles/hr H 2 S. Specified to meet down to %vol H 2 S 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

9 Vacuum Distilation Unit VDU (Added) HISTORY XXXX UNIT CAPACITY Fluid Catalytic Cracker FCCU (Added) HISTORY XXXX UNIT CAPACITY 13,000 BPSD Heavy Gasoil: 86,7 m3/hr Feed ConCarbon wt%

10 ADDITIONAL INFORMATION ABOUT PROCESSING UNITS REVELANT UDGRADES 1. ATMOSPHERIC CRUDE DISTILLATION UNIT a) Capacity: 100,000 BPSD b) Whose technology: Socony Mobil Oil, installed by Foster Wheeler c) Year of relevant upgrade: 1992 ENCON Project Phase ENCON Project Phase Atmospheric Tower Modification 2. NAPHTHA CATALYTICAL HYDRODESULFURIZATION UNIT a) Capacity: 24,000 BPSD b) Whose technology: Socony Mobil Oil, installed by Foster Wheeler c) 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 BPSD b) Whose technology: Socony Mobil Oil, installed by Foster Wheeler c) Year of relevant upgrade: 1991 De-bottlenecked to 14,000 BPSD 1996 New recycle gas compressor was taken into service.

11 4. KEROSENE CATALYTICAL HYDRODESULFURIZATION UNIT a) Capacity: 12,000 BPSD b) Whose technology: Socony Mobil Oil, installed by Foster Wheeler c) Year of relevant upgrade: 1969 Expanded to 12,000 BPSD Kerosene 1988 Modified for gasoil desulphurisation at 10,000 BPSD 1999 De-bottlenecked to 12 TBD with gas oil 5. LIQUEFIED PETROLEUM GAS UNIT a) Capacity: 4,000 BPSD b) Whose technology: Socony Mobil Oil, installed by Lummus d) 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: m3/h fuel gas b) Age: 13 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None. 7. SULFUR RECOVERY UNIT a) Capacity: 20 ton/day of liquid sulfur b) Age: 13 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None.

12 8. SOLID SULFUR FORMING UNIT ( FLAKER ) a) Capacity: 30 ton/day of sulfur flakes b) Age: 9 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None. 9. VACUUM DISTILATION UNIT a) Capacity: 4,000 BPSD b) Whose technology: Socony Mobil Oil, installed by Lummus d) 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: m3/h fuel gas b) Age: 13 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None. 7. SULFUR RECOVERY UNIT a) Capacity: 20 ton/day of liquid sulfur b) Age: 13 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None.

13 8. SOLID SULFUR FORMING UNIT ( FLAKER ) a) Capacity: 30 ton/day of sulfur flakes b) Age: 9 years old c) Whose technology: Snamprogetti d) Year of recent upgrades: None. OTHER PROCESS UNITS CAN BE ADDED DEPENDANT ON CUSTOMERS PRODUCT REQUIREMENTS (i.e. ANOTHER FCCU OR VACUUM DISTILLATION UNIT)

14 3. Feedstock & Products CUTS ASTM end point C Light products Isa naphtha 71 swing stream # 1 82 minimum gasoline swing stream # h s e naphtha 154 swing stream # maximum gasoline swing stream # swing stream # kerosene 271 jet A 1 kerosene 310 product kerosene swing stream # diesel gas oil 388 swing stream # swing stream # residuum 410

15 Crude Oil Throughput History Between (1 Q) x 1000 Metric Tons per Year Year: (Q1) Crude Oil Input Gravity API Indigenous Mix Forozan Kerkuk , E. Sider Iranian Heavy Urals , Syrian Light Saharan Syrian Blend , Iran. Light Basra Light Siberian Light Didon Arabian Light Arabian Heavy Arabian Medium Maya Ras Gharip Brent Tengiz Zueitina Total 3, , , , Import H.F.O Additives Total Input 3, , , ,

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 Gasoline 299.1 317.

16 Production History Between (1 Q) Refinery Production (1 Q) LPG Premium Gasoline Regular Gasoline Unleaded Gasoline Jet A Kerosene All Purpose Diesel 1, , , Home Heating Oil No. 6 Fuel Oil 1, , , , Flaked Sulphure Naphta Total Saleable 3, , , , Unfinished Product

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

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

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

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

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

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

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

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

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

26 REFURBISHED OIL REFINERY FOR SALE AND RELOCATION Ref.-No.: ProOil-276 Thank you! Sonnenberger Strasse Wiesbaden, Germany Tel Fax

20,000 bpd CRUDE OIL REFINERY FOR SALE AND RELOCATION

Ref.-No.: ProOil-278 20,000 bpd CRUDE OIL REFINERY FOR SALE AND RELOCATION Presented by: Lohrmann International Germany FACTS The Refinery was built at 20,000 BPD by UOP/Chyoda in 1974 and mothballed in