Punjtan recycling renewable fuels profile 2012

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Punjtan recycling renewable fuels profile 2012

  1. 1. Renewable Energy FuelsINNOVATIVE RECYCLING OF WASTE HYDROCARBONS TO USEFUL FUELS …innovative solutions for a sustainable future TM
  2. 2. Presentation Overview Who We Are Market niche Intellectual Property Margins and ROI R&D Facility Business Model Sales & Distribution Manufacturing Capacity and Facilities Confidential and Proprietary 2
  3. 3. Who We Are Business: – Turnkey projects in used oil refining and renewable energy. Offices – Headquarters: Houston, Texas, USA – Overseas offices: – Mexico – Veracruz – Bogota – Colombia – Dubai – UAE – Lagos - Nigeria Facilities: – Manufacturing: USA & Other Countries – R&D: USA & CANADA Confidential and Proprietary 3
  4. 4. Business Focus Harvesting energy from hydrocarbon waste streams – Petroleum Sludge & Waste ( Hazardous Material ) – Oil Refineries & Oil Tankers Waste Oil – Waste Plastics – Used Tires – Used Motor Oils – Used Vegetable Oils – Bitumen – Asphalt - Tar-sands – Residual Fuel Oil & Waste – Heavy Thick Crude Oil Confidential and Proprietary 4
  5. 5. Refinery Waste 83% Fuels, Lube Oils and Industrial Products 16% Refinery Residue 5.1B gal/year globally primarily disposed off in open pits! Confidential and Proprietary 5
  6. 6. Waste Plastic 5% Recycled 95% Land Filled 64 B Pounds Annually in USA! 75% of which is industrial Confidential and Proprietary 6
  7. 7. Solution Low-Sulfur Diesel D2 Carbon Black LP Gas Confidential and Proprietary 7
  8. 8. The Underlying Magic Polymer Hydrocarbon Innovative Recycling Process Monomers Catalyst-assisted re-bonding Confidential and Proprietary 8
  9. 9. Technology Attributes Feedstock – Any petroleum, plastic or plant-based oil Preparation – Simple Melting Catalyst – Non-consumable Quality – High / Meets Standards Emissions – None - Closed-Loop Technology Scalability – Aircraft Carrier to Refinery Confidential and Proprietary 9
  10. 10. Competition Environmental Pressure Dumping Opportunity Cost Blending Residue Kerosene Bunker Fuel Pyrolysis Synthetic Gas Fuels Heat Energy Unproven Economics Confidential and Proprietary 10
  11. 11. Existing Innovative Refining Plants Shade from Outside Confidential and Proprietary 11
  12. 12. Existing Innovative Refining Plants Side view showing all skids Confidential and Proprietary 12
  13. 13. Existing Innovative Refining Plants Storage & Processing Tanks Confidential and Proprietary 13
  14. 14. Existing Innovative Refining Plants Confidential and Proprietary 14
  15. 15. Existing Innovative Refining Plants Pre-packaged equipment skid Confidential and Proprietary 15
  16. 16. Existing Innovative Refining Plants Outside view Confidential and Proprietary 16
  17. 17. Existing Innovative Refining Plants Liquids Processing Tanks Confidential and Proprietary 17
  18. 18. Existing Innovative Refining Plants Pre-packaged skids Confidential and Proprietary 18
  19. 19. Existing Innovative Refining Plants Walk way Confidential and Proprietary 19
  20. 20. Existing Innovative Refining Plants Confidential and Proprietary 20
  21. 21. Pilot Scale for R&D and Demo Pilot Plant at USA Continuous Mode – 0.5MT/Day Batch Mode – 6 Trials/Week Fully equipped lab facility Confidential and Proprietary 21
  22. 22. MarketResidue $357 B 717 Refineries Globally, 132 in USA 174 B Gallons – Yields 139 B Gallons DieselPlastic $18.8 B 64 B LB Plastic Waste Land Filled Annually 7.35 B Gallons of Diesel +80% is Industrial (easy to grab) 20,000 Plastic Molders 1,754 Landfills in USB = Billions of Gallons Oils / Fuels from Refineries – Billions of Pounds Plastic from Consumers’ Waste Confidential and Proprietary 22
  23. 23. Sales & Distribution World Oil Refineries Output Confidential and Proprietary 23
  24. 24. Heavy Fuels Confidential and Proprietary 24
  25. 25. Enhanced Oil Recovery Front-End Engineering Design (FEED Studies) AFE Estimated for Overall Project cost Including Installation Mature Production Field Re-development Co2 Capture Facilities including COS (carbonyl sulfide) and H2S (hydrogen sulfide) Removal Pipeline Engineering, Compliance and Project Management HYSY Process Modeling and Heat Load Studies Power Capacity Assessments and Heat Load Studies Cause and Effect Diagrams Process Equipment Design Facility 3D Modeling, Including Piping and Equipment Plans with Isometrics Structural and Civil Design Electrical and Instrumentation Procurement Services Confidential and Proprietary 25
  26. 26. Oil Production Optimization Challenge: High paraffin wells, with high water content Process: Down hole chemical product injection Crude Properties: – API Gravity of 28o – Pour Point of 100oF – Paraffin content of 11% – Asphaltenes content of 4% Results: – 100% increase in production leveling off to Heavy Crude Oil Production 50%  Challenge: Highly viscous, extra heavy – The water cut in the oil that was produced crude oil creating flow challenges was reduced by 95%  Crude: API gravity of 7oto 8o – Please see graphics of results in following  Viscosity: 115,000 to 120,000 Cps@ slides/pages. 40oC  Process: Downhole injection and/or applied in conjunction with steam injection, as well as injection into pipelines and flow stations  Results: API gravity increased to 17o  Viscosity reduction of 60% Confidential and Proprietary 26
  27. 27. Water Recovery for Steam Injection Secondary Recovery Challenge: Resulting emulsion from  Challenge: Declining production SAG-D (Steam Assisted Gravity-  Crude Case 1: API gravity of 12oto 19o Drainage) leaves the ground at 180oC  10 wells with artificial lift and contains 70% water and 30% Bitumen. All of the water has to be  Crude Case 2:API gravity of 32oto 38o recovered.  25 wells with artificial lift Crude: API gravity of 11oto 12o  Crude Case 3:API gravity of 40oto 42o Process: Applied in conjunction with  15 wells with artificial lift steam injection into the massive Canadian tar sands to bring up an  Process: Downhole injection and emulsion of water and Bitumen circulation Results: Using the patented chemicals  Results: Production increase average of they can recover 100% of the water. 35% The recovered water is 100% oil free. The recovered Bitumen has a B.S.&W. of < 0.1%. The sand is totally oil free. Confidential and Proprietary 27
  28. 28. Additional Consideration for Users Our chemical patents were originally developed for cleaning oil refinery and oil reserve tank bottoms; i.e. creating a chemical that would allow for the recovery of the hydrocarbons in the sludge oil. This has been deployed in numerous storage tank facilities around the US and worldwide with a minimum reported recovery rate of 95%. The recovered hydrocarbons are then processed in Oil Refineries. This application would be of tremendous value to any organization seeking Heavy Oil Solutions. The chemicals were discovered to have additional properties that were further adjusted and developed for the uses discussed in the previous cases and considered environment friendly. Confidential and Proprietary 28
  29. 29. Current Users of the Technology Conventional Production (API gravity 18oto 40o+) Production of Heavy Oil (API gravity 7oto 14o)Case StudiesThese are the Oil Companies that have used this technology successfully and areHappy with their Production Enhancement and Maximum Output of their heavyOils & Sand Segregations. Confidential and Proprietary 29
  30. 30. Hydro-Carbon Oil Refineries Confidential and Proprietary 30
  31. 31. Project Experience by Sector: Refinery Hydrocracker Unit Project –Multi-discipline engineering, design, drafting, project management, construction management and coordination of a new Hydrocracker Unit to increase the capacity of an existing refinery by an additional 50,000 BPD. Crude / Vacuum Unit Expansion Project –Multi-discipline engineering, design, drafting, project management, construction management and coordination of a new 50,000 BPD Crude and Vacuum Unit. Mobil Source Air Toxics (MSAT II) Project –Multi-discipline engineering, design, drafting, project management and construction coordination to install facilities to reduce Benzene content in gasoline to meet new environmental regulations. MSCC Expansion Project –Multi-discipline engineering, design, drafting, project management, construction management and coordination of modifications to convert an existing Milli-Second Catalytic Cracker to Fluidized Catalytic Cracker to improve efficiency and quality of the unit, Ultra-Low Sulfur Diesel Project –Multi-discipline engineering, design, drafting and project management of new facilities to reduce the sulfur content in road-grade diesel to meet government mandated sulfur emissions. Sulfur Storage and Handling Expansion Project –Multi-discipline engineering, design, drafting and project management of facilities necessary to increase the sulfur storage and handling capacity of an existing refinery; project scope required design of a 10,000 barrel externally steam traced sulfur tank, sulfur shipping pumps, truck scales and loading racks. ROSE (Residuum Oil Supercritical Extraction) Oil Heater Improvements Project –Multi-discipline engineering, design, drafting and project management of equipment necessary to improve the heating efficiency of the ROSE Oil Heater to reduce energy consumption of the unit; project scope required design of a new air pre-heater, induced and forced draft fans, air ducts and associated instrumentation and controls. Asphalt Handling Expansion Project –Multi-discipline engineering, design, drafting and project management of facilities necessary to increase the asphalt off-loading of the refinery; project scope included installation of new API 610 asphalt transfer pumps, approximately 5,000 feet of 16” electrically heat traced piping from the tank farm to the loading docks, loading arm, associated instrumentation / controls and power requirements Confidential and Proprietary 31
  32. 32. Mechanical/Facilities Engineering Front-End Engineering Design(FEED)Studies Tank Storage/Terminal Facilities Debottlenecking Studies Pipelines and Pipeline Support Facilities Compressor/PUMP Stations Complete Package Process Systems Oil/Gas Dehydration-Treating Produced Water Treating Gas Production, Treating and Compression Crude Oil Processing/Refining Vent/Flare Relief Systems P&ID Development Piping Design and Stress Analysis Pressure Vessel Design Cause and Effect Diagram CO2, Water, Nitrogen and Polymer Injection EOR Facilities Gas Processing Plant and Fractionation Facilities Gas Storage Facilities Gas Gathering Pipeline Systems Pipeline Vital Records and Compliance Records Management Confidential and Proprietary 32
  33. 33. Civil & Infra-Structural Engineering Site/Infrastructure Development Concrete Foundation Design(Pile, Slabs, Footings, etc.) Lift Analysis (Including Rigging Assemblies) Pile Drivability Analysis Feasibility Study/Structural Analysis/Design Process Skid/Module Design Quarters Building Design Load-out and Transportation Engineering Platform Assessment and Mitigation CVA for MMS/BOEMRE (Certified Verification Agent) Floating Structures, TLP, Truss Spars Confidential and Proprietary 33
  34. 34. Instrumentation/Electrical Engineering Lighting System Design Electrical Distribution System Design Motor Control and Switchgear Design High, Medium and Low Voltage Distribution Peak Shavings Design Demand Low Flow and Short Circuit Studies Motor Starting Analysis Protective Coordination Studies Transient Stability Studies Natural Gas, Diesel and Turbine Driven Generator Sets Variable Speed Drive Systems Auto-Synchronization Design Substation Design Instrument Device Specifications Onshore / Offshore Control Systems Design: Electrical, Electronic, Pneumatic and Hydraulic Telecommunications and SCADA Design PLC/DCS Programming & Screen Builds Natural Gas, Diesel and Turbine Driven Generator Sets Complete Process/Equipment Automation Remote Monitoring and Control Confidential and Proprietary 34
  35. 35. Design/Drafting Multi disciplined Design and Drafting ADEPT – Document Control Services Onsite field trips collecting data for facility design and/or retrofit of equipment 3d Model Presentation and Walk-thru Utilizing the Industries latest Drafting Software Confidential and Proprietary 35
  36. 36. Partial List of our Alliance Members Confidential and Proprietary 36
  37. 37. CapabilitiesProject /Construction Management Procurement & Financial Support Strategic Planning and FEED Study  RFQ/RFI Package Class 1 thru 5 Cost Estimating/AFE Development  Competitive bid process management Regulatory Compliance  Cost Tracking/AFE Development Development of Permit Packages for  Cost vs. Time analysis Regulatory  Purchase Order Creation/Issue Submittal Project Cost and Schedule Packages for  Technical bid analysis Regulatory  Cost Control and Loss Reporting Submittal Reporting / Project Metrics  Total Procurement System Management Construction Oversight  Financing of Turn-Key Project Facility Commissioning, Start-up Procedures and Start-up a  Joint Ventures – Partners Identification assistance  Production Marketing & Sales Post Project Documentation  Hydrocarbons Oil & Gas Production Turnaround Planning & Support  barter or trade off ’s for our Services Surveying Process Safety Management (PSM) Confidential and Proprietary 37
  38. 38. Contact Information Innovative Recycling of Waste Hydrocarbons to Useful fuels 11777 Katy Freeway, Suite 138 Houston, Texas 77079 USA Tel: +1 (713) 266-7447 Fax: +1 (713) 588-2411 Mobile +1 (713) 581-4505 Email: jack@a1oilandgas.com OR services@punjtanenergy.com Confidential and Proprietary 38

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