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Advanced Gas Separation Systems using Polymeric Membrane Technology 5 th  Annual Angel Investor Summit Ottawa, October 24, 2005
Investment Highlights ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Company Profile ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Vaperma’s Solution ,[object Object],[object Object],[object Object],[object Object],High Selectivity of Water and H2S
50 kg/h Module and Dehydration System
Markets & Value Proposition Vaperma Technology Advanced Dehydration Process Solutions based on vapor-phase membranes Markets ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Value Proposition ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Enhanced Water Gas Shift Reaction
Fuel Ethanol Dehydration Solution:   Vaperma membranes provide an attractive solution to traditional distillation/molecular sieve unit (MSU).  In combination with mechanical vapor recompression units, Vaperma Advanced Ethanol Dehydration Process Solution save as much as 40% on operating costs. ($2.9M energy savings for a 160 ML/yr world-class plant) Problem:   In a typical corn-based ethanol plant, the beer from the fermentation process contains 8 to 12 % ethanol. In a cellulose-based ethanol plant, the beer ethanol concentration is 4%.   Cost:   The capital investment required for the installation of a dehydration system in a 160 ML/yr plant is approximately $23M USD with annual energy expenses of $6.8M for a modern ethanol plant and up to $9.8M for conventional ethanol plant or 4.2 and 6.1 cents per liter respectively.
Traditional Distillation/MSU Process 40% ETHANOL 90% ETHANOL
Traditional Distillation/MSU Process 40% ETHANOL 90% ETHANOL
Sour Gas Treatment Problem:   Water and H2S are common impurities in natural gas that must be removed to meet pipeline specifications and prevent hydrate formation. Solution:   Vaperma membranes provide an attractive solution to traditional glycol systems based on simple process designs, lower costs, lightweight and compact assembly.  Ideal for remote locations with limited utilities.  The membranes are suitable for a variety of offshore and onshore applications. Advantages:   Vaperma membranes offers higher water and H2S selectivity and higher temperature over existing PRISM membrane technology. Market Focus:   Natural gas fields (sour gas) of 10,000 to 20,000 Nm3/h operated by small pipeline head operators (Large fields are 50,000 to 150,000 Nm3/h).
Financial & Strategic Partners VC’s & Angel Investors Private Industry Partners Institut français du pétrole
Experienced Management Team Senior R&D engineer, Pyrovac Senior Process Engineer Bruno de Caumia Senior R&D engineer, Pyrovac Senior Process Engineer Pierre Plante Polymer scientist, Polymer Research Institute, Chengdu, China  R&D Scientist Jingui Huang Membrane specialist, Pyrovac & Laval University VP R&D Richard Cranford President & CEO, Kontron Communications & Avestor Chairman & CEO Claude Letourneau Prior Experience Title Name
 
Vaperma’s Vision ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Protected Technology ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Fuel Grade Ethanol Value Chain  ,[object Object],Raw Material Supplier MSU or Membrane Supplier Dehydration Technology Provider Ethanol Technology Provider EPCM Ethanol Producer Fuel Producer Vaperma Business Licensee or Partner ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Oil & Gas
Commercialization Strategy - Ethanol Membrane Cartridges & Dehydration Systems Turn-Key Plants Value-added $0.4M  US $23M  US $150M  US Cartridges Membranes Modules Dehydration Plant Ethanol Plant $3M  US Membranes Systems $6M  US 160 ML/yr plant Newco MJV Ethanol Dehydration Membrane Technology Provider Ethanol Technology Provider Ethanol Producers EPCM
Business Strategy ,[object Object],[object Object],[object Object],[object Object],[object Object]
Ethanol Dehydration Roll-out Plan Phase 2 : 1600 kg/h (40% Feed) Field Testing at CAI 2004 2008 Phase 1A :   50 kg/h (90% Feed) Field Testing at CAI 2005 2006 2007 2009 2010 Phase 1B : 100 kg/h (40% Feed) Field Testing at cellulose plant Field Testing Field Testing Field Testing Commercial Launch 15,000  - 20,000 kg/h 20 m2 per module 100 m2 per module Membrane module manufacturing development 100 m2 per module 50 kg/h Bench Unit 20 m2 (one cartridge) TEAM Project SDTC Project
Financing Plan
Funding Gaps Source: SDTC Innovation Chain Risk Profile Funding Intensity SDTC TEAM IRAP / CANMET
Seed Funding History ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],$1.4 millions invested to date
TEAM Funding Experience ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Enhanced the stature and credibility of Vaperma in the industry
Offering Summary ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

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Summit 05 Presentations 06c Letourneau

  • 1. Advanced Gas Separation Systems using Polymeric Membrane Technology 5 th Annual Angel Investor Summit Ottawa, October 24, 2005
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  • 5. 50 kg/h Module and Dehydration System
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  • 7. Fuel Ethanol Dehydration Solution: Vaperma membranes provide an attractive solution to traditional distillation/molecular sieve unit (MSU). In combination with mechanical vapor recompression units, Vaperma Advanced Ethanol Dehydration Process Solution save as much as 40% on operating costs. ($2.9M energy savings for a 160 ML/yr world-class plant) Problem: In a typical corn-based ethanol plant, the beer from the fermentation process contains 8 to 12 % ethanol. In a cellulose-based ethanol plant, the beer ethanol concentration is 4%. Cost: The capital investment required for the installation of a dehydration system in a 160 ML/yr plant is approximately $23M USD with annual energy expenses of $6.8M for a modern ethanol plant and up to $9.8M for conventional ethanol plant or 4.2 and 6.1 cents per liter respectively.
  • 8. Traditional Distillation/MSU Process 40% ETHANOL 90% ETHANOL
  • 9. Traditional Distillation/MSU Process 40% ETHANOL 90% ETHANOL
  • 10. Sour Gas Treatment Problem: Water and H2S are common impurities in natural gas that must be removed to meet pipeline specifications and prevent hydrate formation. Solution: Vaperma membranes provide an attractive solution to traditional glycol systems based on simple process designs, lower costs, lightweight and compact assembly. Ideal for remote locations with limited utilities. The membranes are suitable for a variety of offshore and onshore applications. Advantages: Vaperma membranes offers higher water and H2S selectivity and higher temperature over existing PRISM membrane technology. Market Focus: Natural gas fields (sour gas) of 10,000 to 20,000 Nm3/h operated by small pipeline head operators (Large fields are 50,000 to 150,000 Nm3/h).
  • 11. Financial & Strategic Partners VC’s & Angel Investors Private Industry Partners Institut français du pétrole
  • 12. Experienced Management Team Senior R&D engineer, Pyrovac Senior Process Engineer Bruno de Caumia Senior R&D engineer, Pyrovac Senior Process Engineer Pierre Plante Polymer scientist, Polymer Research Institute, Chengdu, China R&D Scientist Jingui Huang Membrane specialist, Pyrovac & Laval University VP R&D Richard Cranford President & CEO, Kontron Communications & Avestor Chairman & CEO Claude Letourneau Prior Experience Title Name
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  • 17. Commercialization Strategy - Ethanol Membrane Cartridges & Dehydration Systems Turn-Key Plants Value-added $0.4M US $23M US $150M US Cartridges Membranes Modules Dehydration Plant Ethanol Plant $3M US Membranes Systems $6M US 160 ML/yr plant Newco MJV Ethanol Dehydration Membrane Technology Provider Ethanol Technology Provider Ethanol Producers EPCM
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  • 19. Ethanol Dehydration Roll-out Plan Phase 2 : 1600 kg/h (40% Feed) Field Testing at CAI 2004 2008 Phase 1A : 50 kg/h (90% Feed) Field Testing at CAI 2005 2006 2007 2009 2010 Phase 1B : 100 kg/h (40% Feed) Field Testing at cellulose plant Field Testing Field Testing Field Testing Commercial Launch 15,000 - 20,000 kg/h 20 m2 per module 100 m2 per module Membrane module manufacturing development 100 m2 per module 50 kg/h Bench Unit 20 m2 (one cartridge) TEAM Project SDTC Project
  • 21. Funding Gaps Source: SDTC Innovation Chain Risk Profile Funding Intensity SDTC TEAM IRAP / CANMET
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