Exclusively offered by: Lohrmann International GmbH Sonnenberger Strasse 16 Tel. +49 611 701888 www.lohrmann.com 65193 Wiesbaden (GERMANY) Fax +49 611 701895 info@lohrmann.com
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 2.1 - Products & specifications 2.2 - Scope of supply & services 2.3 - Layout & required space 2.4 - Commercial and economical evaluations 2.5 - Cost comparison 2.5.1 - Budgetary offer total investment estimation 2.5.2 - Estimated return of invest and costs 2.5.3 - Approach 2.6 - Timing 2.7 -Actions 2.8
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 2008. 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 2008. 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.
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.
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 1965 1989 5430 1950000 39000 Crude Distill. (version2) N.A. 1965 1989 11100 4000000 80000 Hydrotreat (Unifiner) UOP 1965 2004 1130 410000 8100 Amin-Regeneration and Sour Water Stripper N.A. 1965 530 190000 3800 Sulfur 1 Lurgi 1965 2006 13 5000 100 LPG-Rec/ C3+-Rec/Splitter N.A. 1965 260 each 95000 1900 Fluid CatalyticCracker (FCC) UOP 1993 2650 955000 19100 Hydrobon UOP 1975 2003 3360 1210000 24200 Dehexanizer UOP 2003 2880 1040000 20800 Contin. Reformer(CCR) UOP 1975 2040 740000 14700 Isomerization (Penex/DIH) UOP 1975 1440 520000 10400 Sulfur 2 Amoco 1978 1993 17 6000 120 MD-Desulfurization(HDS) Snamprogetti 1978 2520 910000 18200 UTILITY UNITS: Cooling Water System N.A. 1965 1975 36000 Waste Water Treatment Lurgi 1965 2005 3600 Hotoil-System/ Steam Gen. UOP 1965 1975 8640 Nitrogen/ Plant& Instr.Air N.A. 1965 1975
2.2 Product Yields/ Specifications Products Cap. Mt/a x1000 Cap. Mt/a x1000 Product Specification Current Oper. Alternate Oper. Motor Gasolines 2000 1750 EN 228, issue 2005 Diesel 870 1100 EN 590, issue 2005 Kerosene (Jet Fuel) 75 100 Refinery Spec. Fuel Oil 100 120 ISO 8217/ IMO & EU directive Heavy Fuel Oil 500 380 ditto LPG 75 60 EN 589 Ref. Gas (Fuel Gas) 60 50 Refinery spec. Hydrogen 1.7 1.5 Refinery spec. Sulfur 10 60 Refinery spec.
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 51 Density @ 15 C, kg/m3 845 Distillation, T95 C, max 360
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
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 )
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
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
SCOPE - Complementary Supplies / Materials (when transfered) Assumptions In Sales Price (SP) To complement Equipment 100 % 0 % Civil & Buildings 0 % + 100 % Piping 80 % + 20 % Structural Steel 80 % + 20 % Instrumentation 30 % + 70 % Electrical 50 % + 50 % Insulation/Painting/Fire Protect. 0 % + 100 %
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
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
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
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
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
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
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
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
Thank you for your attention. Related Webpage: www.used-refinery.com Lohrmann International GmbH Sonnenberger Strasse 16 Tel. +49 611 701888 www.lohrmann.com 65193 Wiesbaden (GERMANY) Fax +49 611 701895 info@lohrmann.com