Realizing The Full Potential From Bitumen and Heavier Crudes I Y Q Upgrading February 2013
Advisory This presentation contains statements that may constitute "forward-looking statements" within the meaning of applicable securities legislation. These statements include, among others, statements regarding business strategy, beliefs, plans, goals, objectives, assumptions or statements about future events or performance. By their nature, forward looking statements are subject to numerous risks and uncertainties, some of which are beyond ETX System's control, including the impact of general economic conditions, industry conditions, volatility of commodity prices, currency fluctuations, environmental risks, competition from other industry participants, lack of availability of qualified personnel or management, stock market volatility and ability to access sufficient capital from internal and external sources. Readers are cautioned that the assumptions used in the preparation of such information, although considered reasonable at the time of preparation, may prove to be incorrect and, as such, undue reliance should not be placed on forward looking statements. Actual results, performance or achievement could differ materially from those expressed in, or implied by any forward looking statements in this presentation, and accordingly, no assurance can be given that any of the events anticipated by the forward looking statements will transpire or occur, or if any of them do so, what benefits ETX Systems will derive there from. All of the forward-looking information and statements contained in this presentation are qualified by these cautionary statements. The reader of this presentation is cautioned not to place undue reliance on any forwardlooking information and statements. ETX expressly disclaims any intention or obligation to update or revise any forward-looking information and statements, whether as a result of new information, events or otherwise, except in accordance with applicable securities laws. Non-Solicitation This presentation does not constitute or form part of any invitation, offer for sale or subscription or any solicitation for any offer to purchase or subscribe for any securities of ETX nor shall they or any part of them form the basis s of or be relied ed upon inconnection o therewith e t or act as any inducement e to enter into any contract or commitment t with respect to such securities. es The information o contained herein e was not prepared edin connection o with an offering of securities and in no way constitutes an offering memorandum for the purposes of applicable securities law. Further, this presentation is for informational purposes only and must not be used or relied upon for the purpose of making any investment decision or engaging in any investment activity. Neither ETX nor any of its directors, officers, employees, agents or advisors make any representation or warranty in respect of the contents of this presentation or otherwise in relation to ETX or any of its respective businesses. In particular, no representation or warranty, express or implied, is made as to the fairness, accuracy or completeness of the information or opinions contained herein, which have not been independently verified. No person shall have any right of action (except in case of fraud) against ETX or any other person in relation to the accuracy or completeness of the information contained in this presentation. The information containedin this presentation is provided as at the date hereof and is subject to amendment, revision and updatingin any way withoutnotice or liability to any party. Certain information contained herein has been prepared by third-party sources. The information provided herein has not been independently audited or verified, by ETX. ETX has used its best efforts to ensure the accuracy and completeness of the information presented. 2
Executive Summary I Y Q Upgrading g by ETX Systems Emerging technology for Primary Upgrading (coking) of heavier crudes Industry-altering ability to maximize yield of premium refinery feedstock Patent t protected, t with lower cost and environmental footprint t Progressing final development step - a 1,000 bpd Field Pilot Growth in oil sands requires significant new investment in coking capacity $75+ million / day of upside currently being forfeited with dilute and ship New coking capacity is required to address structural basis for collapse I Y Q Upgrading is positioned to capitalize Addresses pricing, pipeline and environmental challenges to future growth Unlocks $10/bbl of new value with every barrel of bitumen processed 3
The Role of Coking Technologies Primary Upgrading: Converts non-distillable bottom portion of a crude oil barrel into refinery feedstock, rejecting impurities in the process Heavy oil and bitumen contain more non-distillable components than light oil Coking is particularly important for getting full value from heavier crudes Production Primary Upgrading Secondary Upgrading Refining 100 50 0 Percent Pitch Distillate + Gasoil PUG converts pitch fraction Sulfur 4
Coking Landscape Delayed Coking: currently the over-whelming choice of industry Mature, with decades of commercial experience, but far from ideal Fails to maximize liquid yields, impairing economics and increasing environmental impact of bringing heavier crude to market I Y Q Upgrading has been rigorously benchmarked against delayed coking Significant increase in distillable liquids from same barrel of feedstock Lower Capital, Operating costs 5
I Y Q Upgrading g How We Do It Patented I Y Q Upgrading approaches ideal coking Combination o of two ocommercially eca ypo proven technologies ooges Plug-flow dryers Fluid bed coking Liquid feed Fluidization gas and reaction products I Y Q Upgrading closes the gap Hot solids Cool solids 100 Fluidization gas (wt%) Yield 90 80 70 Gas Coke Liquid 60 Delayed Coking "Ideal Coking" 6
ETX Executive Gerard Monaghan (PEng, MBA), CEO A decade of front line experience with Syncrude / Exxon ER&E Leading edge exposure to advances in fundamental understanding of Upgrading science Wayne Brown (PEng, PhD), CTO 25 years of experience orchestrating ti and executing top tier development Demonstrated track record through staff positions with both industry (Syncrude) and academia (McGill) Awarded 2011 ASTECH Prize for Innovation in Oil Sands Research Bernie LeSage (MEng, MBA), COO 30 years of experience in technology development and commercialization Significant international marketing and operations experience Combined 40 years of experience covering most major Integrated Oil Sands projects 7
The Team Demonstrated ability to align with world class individuals and organizations oga a o Independent Directors George Crookshank Energy Consultant Keith MacLeod President, Sproule Associates Sean Monaghan President, Promac Industries Randy Ollenberger Managing Director, Research, BMO 8
Incremental Benefits An Oil Sands Example Relative to delayed coking, I Y Q Upgrading provides: $10+/bbl of new value for every barrel processed Direct 9% reduction of upstream environmental intensity metrics $1+ Billion of incremental NPV12 for typical commercial rollout $12 I Y Q Advantage vs. Delayed Coking* $10 ue $/bbl Incremental Val $8 $6 $4 $2 $0 Liquid Yield Advantage Operating Advantage Capital Advantage Netback Advantage * When processing whole Athabasca bitumen, $75 WTI 9
Development Activities Conception Feasibility Process Piloting Commercialization Development 10
Field Pilot Project Last development step is to execute a 1,000 bpd Field Pilot project to demonstrate operability of I Y Q Upgrading Carrying $95 million as all-in cost, based on Design Basis Memorandum completed in 2012 for a Central Alberta location Scrubber Hot box from 1,000 bpd Field Pilot Design Basis Memorandum Heater Expect significant support Reactor from Government, based on advanced discussions 11
Why Invest in Primary Upgrading (Coking)? The next big opportunity in Oil Sands Investment! Have reached a tipping point for continental coking infrastructure Increasing ability to source suitable feedstock (linked to oil sands growth) has overwhelmed current and planned coking capacity Until balance is restored, incremental bitumen is stranded, pricing is distressed Expect premium investment returns from new coking projects over this period US Coking Capacity Versus Coking Inputs 3,000,000 100.0% ls Per Calendar Day Barrel 2,500,000 2,000,000 1,500,000 1,000,000 500,000 Ability of refiners to source discounted feed increases as Utilization exceeds 90% 95.0% 90.0% 85.0% 80.0% 75.0% Utilization - 1999 2000 2001 2002 2003 2004 2005 2006 2007 2008 2009 2010 2011 2012 2013 2014 2015 70.0% Year Capacity Actual Capacity Forecast Inputs Actual Inputs Forecast Actual Utilization Forecast Utilization 12
Opportunity Continues to Grow Increasing demand for refined products and robust economics for increasing supply of heavy oil will drive new investment in coking Coupled with limited ability of coking infrastructure to accommodate current supply, expect massive investment over extended periods to bring market back into balance Golden Age of Upgrading Productio on (Mbbl/d) Global Heavy Oil Production 20,000 15,000 10,000000 5,000 0 2010 2015 2020 2025 2030 2035 North America South America Europe, Russia,& Central Asia Asia Pacific Middle East Africa Production (Mbbl/d) Canadian Oil Sands Production 6,000 5,000 4,000 3,000 2,000 1,000 0 2010 2015 2020 2025 2030 Oil Sands Mining Oil Sands In-Situ Hart Energy 2011 Long Term Scenario 2012 CAPP Crude Oil Forecast 13
Why ETX and I Y Q Upgrading? Team, Technology, and Timing Team: Dedicated and Award winning Fundamental grasp of science, front line exposure to Industry needs Demonstrated ability to steward and leverage capital over the past ten years Technology: Doing more, with less. Getting 9% more refinery-ready feedstock from a given barrel of bitumen Less capital and operating cost Industry-altering ability to effect a $10/bbl reduction in the crude pricing i required to support break-even economics for oil sands development Timing: Positioned to capitalize on next big wave of Oil Sands Investment 100+ commercial coking projects (50,000000 bpd) are required to support forecast growth of heavy oil, ETX only needs to convert on one of these (with 10% retention of value created) to recover development costs. Opportunity to convert on additional commercial rollouts provides significant upside 14
Bitumen Pricing: How Low Can It Go? New coking investment is incented by heavy oil discount Despite global crude oil benchmarks that have consistently traded at $100+/bbl in recent years, bitumen at the well head currently receives only a fraction of this At current prices Western Canadian Producers are forfeiting $2- $3 billion / month to midstream / downstream entities 15
Inherent Value in Bitumen Inherent value of bitumen is unlocked with well contemplated strategy to link new bitumen supply to motivated refiners While indications are that it may not last, recent pricing of Mayan crude (global benchmark for heavy crude) is indicative of this inherent value Better technology for coking (I Y Q Upgrading) can add significantly to this inherent value 140 Heavy Oil Pricing Potential 120 100 80 60 US$/bbl 40 20 0 May-1987 Mar-1988 Jan-1989 Nov-1989 Sep-1990 Jul-1991 May-1992 Mar-1993 Jan-1994 Nov-1994 Sep-1995 Jul-1996 May-1997 Mar-1998 Jan-1999 Nov-1999 Sep-2000 Jul-2001 May-2002 Mar-2003 Jan-2004 Nov-2004 Sep-2005 Jul-2006 May-2007 Mar-2008 Jan-2009 Nov-2009 Sep-2010 Jul-2011 May-2012 16 Brent Mayan
Market for New Coking Capacity Strong economic case emerging to consider new coking capacity in lower cost jurisdictions in Alberta (Sturgeon County, Peace River...) Ability to eliminate requirements to source diluent Ability to address heavy oil discount and maximize ROI Ability to reduced imposition on takeaway infrastructure (pipelines) Motivated Government with an ability to improve access to financing for new Upgrading investment Case is aided by the fact that US Refiners are focused on shale oil opportunity rather than new investment to process heavier crudes 17
ETX Revenue Model Focus on maximizing market penetration rather than maximizing retention of upside Licensing to entities that are set up to assume role of project developer Target 10% retention of upside for initial capacity Joint Venture with entities that require or desire assistance in project set up Technology farm in, resulting in equity share in project Royalty Equity ETX Licensing Technology Support Joint Ventures Project Support 18
Valuation and Returns - A Licensing Example Assume successful field pilot, 25 million share float, NPV12 Incremental ~$1 Billion upside with each 1% market penetration Technology royalty allows ETX to retain a portion of upside 450 400 350 NAV ($) / Share 300 250 200 150 Upside Retained 10% 20% 30% 100 50 0 0 5 10 15 20 25 30 35 40 45 50 Market Penetration (%) 19
Summary The dilute and ship strategy that has underpinned current development of oil sands and heavy oil supply Western Canada is busted Strategy failed to provide for critical infrastructure required to support pricing After a successful Field Pilot, I Y Q Upgrading by ETX will be well positioned to become the patent protected backbone of a far more robust strategy designed to maximize returns from production of heavier crudes Returns from commercial capacity expected to justify multi-fold returns to new investors ETX is focused on financing and executing this Field Pilot to unlock value for shareholders h and usher in a new era of economic and sustainable development of heavy crudes. 20