Used Oil Refinery for Sale and Relocation, 80,000 bpd.

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1 Exclusively offered by: Lohrmann International GmbH Sonnenberger Strasse 16 Tel Wiesbaden (GERMANY) Fax

2 AGENDA: Project-introduction and brief description 1. - General Capacities 1.1 -Facts 1.2 -Summary 1.3 The Project 2. - Main units, age, last revamp & capacities Products & specifications Scope of supply & services Layout & required space Commercial and economical evaluations Cost comparison Budgetary offer total investment estimation Estimated return of invest and costs Approach Timing 2.7 -Actions 2.8

3 1. Project-introduction and brief description 1.1 General Capacity The capacity of the refinery is equivalent to 80,000 bpd. (= 4 Mil. MT/a) crude oil feed. Crude Oil was received from the CIS, North Sea, North Africa and West Africa. The Refinery was originally designed for Arabian Light Sweet Crude Oil. 1.2 Facts The refinery is still in full commercial operation and is planned for shutdown mid Location of the refinery is the southern German town Ingolstadt, aprx. 100 km. north of Munich (Airport) Reason for taking this refinery out of operation is solely its close vicinity to the city community with fast growing industrial areas, leading the Owner to extend and complete his refining facilities in other close by locations, coming on-stream mid All of the refining facilities are in best overall and mechanical conditions, proper maintained, and by design fully in line with the development of technology and catalyst requirements, norms and standards of product qualities, and European environmental standards.

4 1.3 Summary To summarize, the above refining facilities are: of best up-to-date European design and safety standards, capable of refining a broad range of feeds ( crude and intermediates ), capable of refining at maximum light end products ( Hydrogen, LPG`s, Gasolines ) capable to operate with high flexibility and at deep conversion. Overall the offer represents an excellent opportunity, to close potential refining gaps, to save valuable lead time ( at least 15 month ) compared to a new refinery complex, apart from the fact considerable investment capital is saved.

5 2. The Project 2.1 Main units, age, last revamp & capacities Below tabulation indicates the Processing Facilities for sale as currently operated. Processing and Utility Units: Units Licensor Year Initial Operation YearLast Revamp Design Cap. MT/d Design Cap. MT/a Design Cap. bpd PROCESS UNITS: Combicracker (version1) Snamprogetti Crude Distill. (version2) N.A Hydrotreat (Unifiner) UOP Amin-Regeneration and Sour Water Stripper N.A Sulfur 1 Lurgi LPG-Rec/ C3+-Rec/Splitter N.A each Fluid CatalyticCracker (FCC) UOP Hydrobon UOP Dehexanizer UOP Contin. Reformer(CCR) UOP Isomerization (Penex/DIH) UOP Sulfur 2 Amoco MD-Desulfurization(HDS) Snamprogetti UTILITY UNITS: Cooling Water System N.A Waste Water Treatment Lurgi Hotoil-System/ Steam Gen. UOP Nitrogen/ Plant& Instr.Air N.A

6 2.2 Product Yields/ Specifications Products Cap. Mt/a x1000 Cap. Mt/a x1000 Product Specification Current Oper. Alternate Oper. Motor Gasolines EN 228, issue 2005 Diesel EN 590, issue 2005 Kerosene (Jet Fuel) Refinery Spec. Fuel Oil ISO 8217/ IMO & EU directive Heavy Fuel Oil ditto LPG EN 589 Ref. Gas (Fuel Gas) Refinery spec. Hydrogen Refinery spec. Sulfur Refinery spec.

7 Note 1) EN 228, 2005 requires gasoline qualtity parameters : Sulfur value in brackets (=10 ppm max ) is 2009 requirement Aromatics, vol%, max 35 Olefins, vol%, max 18 Benzene, vol%, max 1.0 Oxygen,wt%, max 2.7 Sulfur, ppm, max 50(10) RVP, kpa 60/70 Lead, g/l max none Note 2) EN 590, 2005 requires diesel quality parameters : Poly Aromatics, vol%, max 11.0 Sulfur, ppm, max 50/(10) Cetane number, min C, kg/m3 845 Distillation, T95 C, max 360

8 2.3 Scope of Supply & Services Within the offer included: As is / Where is Refinery (version 1.) Dismantling, Cleaning, Preservation, Packing and Labeling/Marking (digital documentation of packing) Loading on Truck Pre- / Basinc Engineering and Process Simulation on the new crude oil Optional: Procurement and supply of complementary materials / Detail engineering Transportation / Construction / Re-assembly / Advisory Start Up Assistance, Training

9 SCOPE - Complementary Process & Utility Units (at new location) Re-Build Combi-Cracker to Crude Distillation ( version 1 ) - current operation as Visbreaker/ Thermal Cracker Add new Crude Distillation as Atmos. & Vac. Distill. ( version 2 ) - alternate operation with full as-built - conversion cap. Complement Process units for materials not subject for transfer to new location - ( like Civil, Buildings, Concrete Structures, Insulation, Painting, Fire Protection ) or partly transfer has to be assumed Complement internal infrastructure (ISBL= utility units ) for new location requirements Add new external infrastructure ( OSBL-facilities )

10 SCOPE - Internal Infrastructure Requirements Flare(s) Incinerator(s) Cooling Towers Fire Fighting Facilities Intermediate Product Tanks Control Rooms Electrical Substations Warehouses, Lab`s Supply Networks w/i Battery Limits (BL) like RW / CW / PA / IA / N / ST / C / HO

11 SCOPE - External Infrastructure Requirements Storage Facilities Pipeline Shipment (to / from Plant) Loading- & Unloading Facilities Power Station & HV Distribution Raw Water Intake Station Administration Building Supply Networks w/i OSBL Roads, Pavements, Trenches, Dikes Fences

12 SCOPE - Complementary Supplies / Materials (when transfered) Assumptions In Sales Price (SP) To complement Equipment 100 % 0 % Civil & Buildings 0 % % Piping 80 % + 20 % Structural Steel 80 % + 20 % Instrumentation 30 % + 70 % Electrical 50 % + 50 % Insulation/Painting/Fire Protect. 0 % %

13 2.4 Layout and Space Layout Consumption (in sq.-meters) Total - Process Units: 280 x 510 m 142,800 m² - Tankage: 944,500 m² - Total: 830 x 1,310 m 1,087,300 m² Tankage (space in cub.-meters) - Total A1 Inventory (Floating Roof Tanks) 670,000 m³ - Total A2 Inventory ( Cone Roof Tanks) 65,000 m³ - Total A3 Inventory ( Cone Roof/ Spheres) 790,000 m³

14 2.6 Approach Approach in Phases Phase 0 Questionaire Refinery Complex Sign Pre-contract (BE/S) Phase 1 Project Specification Sign EPCM- Contract (DE/P/CM) Phase 2 Detail Engineering/ Definition of Complementaries/ Disassembly / Transportation, Sign Supplies- Contract (E/P/CA) Phase 3 Construction Advisory & Start Up Assistance

15 Phase 0 - Questionnaire Refinery Complex Site Information Meteorological Data Plant Definitions (Feedstocks/ Product Qualities/ Utility Requirements/ Environmental & Safety Standards ) Design Definitions (Norms/ Standards/ Units of Measure) Licensor Requirements Update Expose

16 Phase 1 - Project Specification Description of the Project Process Simulations ( new H&MB) Process & Design Criteria Product Slate/ Capacities Site Information/ Meterological Data Feedstock Definitions Product Program & Product Quality Specifications Estimated Utility Demand/ Existing Infrastructure Environmental Impact External Infrastructure Requirements Plot Plan Requirements Investment Cost Project Execution Schedule Financial & Economic Evaluation

17 Phase 2 - Detail Engineering / Definition of Complementary Supplies Complement Existing Documentation Provide Eng. Documentation for New Facilities Provide Project Management Criteria & Tools Establish Inquiries & POR`s for Complementary Supplies Provide Project Execution Plan ( Cleaning / Marking / Material Identification / Dis-assembly / Transport to Seaport and Site / Construction & Re-assembly / -Precommissioning/ Start Up ) Provide Training at Current Location

18 Phase 3 - Construction Advisory / Start Up Assistence Provide Construction Execution Plan Provide Construction Advisory Criteria & Tools Establish Consortium for Site Construction Provide Construction Project Controls Provide Training at Previous Owners Facilities

19 TIMING Project Execution Schedule Milestones (fast track) Questionaire: now Award Pre-Contract: latest 31. March 2007! Project Spec (Phase1): 1. Januar 2007 to 30. September 2007 Award EPCM-Contract: latest 30. September 2007 Detail Eng. (Phase2): 1. October 2007 Procure of Compl. Supplies: 1. April 2008 Plant Shutdown: 30. June 2008 Material Transports to Site: 1. September 2008 to 20. December 2009 Award CASU-Contract (Phase3): 30. March 2008 Construction at Site: 1. April 2008 to 30. November 2009 Commissioning/Start Up: 1. December 2009 to 31. January 2010

20 Contractual Consortium Build Up ( capable EPC-Companies only ) Managing Contractor: Lohrmann International Multiple Contracts: Pre-contract for Phase 1 EPCM-contract for Phase 2 CASU-contract for Phase 3 Contracting Mode: Lumpsum

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26 Thank you for your attention. Related Webpage: Lohrmann International GmbH Sonnenberger Strasse 16 Tel Wiesbaden (GERMANY) Fax