Opportunities & Challenges in Transportation Fuels Production

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Opportunities & Challenges in Transportation Fuels Production Soni O. Oyekan Marathon Oil & Criterion & Sal Torrisi Criterion AIChE Regional Process Technology Conference Galveston, TX October 2, 2009 My presentation was prepared by Sal Torrisi and I and Sal is in the meeting today. The presentation takes a reasonable stab at the opportunities and challenges facing the oil refining sector. Sal will be chiming in and we will be available after the session for additional discussions.

Outline Crude Oil & Bitumen Gasoline Diesel Availability Upgrading and refining Gasoline Low sulfur gasoline Ethanol blending Gasoline benzene Diesel ULSD Biodiesel I plan to cover the sections outlined briefly as each of the three major sections could be the topic of a full symposium. I plan to touch on crude oil availability issues, bitumen production and upgrading. I will also discuss gasoline production in terms of recent developments that have been driven by EPA regulations and other US fuels mandates. After the discussions on gasoline I would then discuss diesel and biodiesel.

US Energy Long Term Challenges Conventional Crude oil Crude oil quality is declining Increased competition – China & India Oil companies and national oil suppliers relationships are evolving Supply disruptions are more frequent Crude oil consumption is expected to increase Greenhouse gas emissions and climate issues are ratcheting up The world’s crude oil daily production stands at stands at about 80 to 88 MM BPD. Of that about 25 % is used in the US. Some of the current challenges with conventional crude oils supply are listed. We are processing more percentages of heavier and sour crude oils as crude oil quality is declining. We face increased competition for oil supply from China and India. We are also fully aware of oil production disruptions in some countries and especially in Nigeria.

Global Oil Reserves By Country (Source: CAPP) The slide shows Saudi Arabia with the largest proven oil reserve of 264 billion barrels and US relatively far behind at 21 to 26 billions of barrel. However, Canada comes in at 179 billion and that places Canada at second place. However, more optimistic experts now believe that with existing bitumen recovery technologies, Canadian oil reserve could exceed 311 billion barrels. Ref: Emerging technologies for producing paraffins, olefins & aromatics, Michael C. Oballa & Vasily Simanzhenkov 4

Bitumen Provides Options Oils Sands: A mixture of sand, crude bitumen, water and clay Typical Composition 10% bitumen 83% sand 7 % water & clay 1 barrel of bitumen is obtainable from 3 to 4 tons of oil sands! Bitumen is an extra heavy, sour, poor quality oil Significant upgrading required 10 % higher GHG generated relative to conventional oil?

Non Facile Commercial Recovery Technologies Surface Mining Steam Assisted Recovery Bitumen has to be recovered from the oil sands. For oil sands that are about 200 ft from the surface, surface mining and extraction is used. For recovery of the bitumen from deeper areas beyond 200 ft, surface mining is not the route and in-situ bitumen recovery is practised. One of those is the steam assisted gravity drainage system. Novel in-situ recovery technologies such as SAGD are expected to help fuel the growth of bitumen recovery to about 3 to 4 MM BPD by 2010. Ref:

Bitumen Pose Significant Challenges Bitumen and fractions have higher contaminants Sulfur distributions reflect more refractory compounds Higher refractory nitrogen Higher TAN (Athabasca 3.5 relative to < 1 for conventional oils) Significantly higher hydrogen consumption Natural gas dependency for fuel and hydrogen High requirement for naphtha Pipeline infrastructure for market accessibility Environmental issues Land reclamation Sour gases and GHG Water conservation Plant flexibility and operating margins could be impacted.

Bitumen Refining Challenges Oil Type Arab Med(1) Mars Maya Hamaca Bitumen(2) Athabasca Bitumen(3) Gravity, API 30.7 28.1 20.9 8.4 7.5 Sulfur, wt. % 2.4 2.2 3.4 3.8 4.8 TAN, mg/g 0.25 0.63 0.32 2.8 3.5 Ni, wppm 4 20 52 115 150 V, wppm 18 46 232 388 290 Marathon crude oil assay database V/Ni ratio a parameter for palaeo-environmental characteristics…., F. Galarraga, et.al., J. Petro. Science, 61, Issue 1, pages 9-14, April 2008 Tutorial on upgrading oil sands bitumen, M. R. Gray, University of Alberta.

Atmospheric Distillation Unit Vacuum Distillation Unit Naphtha-Jet Distillates N-J HDT Distillate HDT SCO SCO to Refinery VGO HDT Atmospheric Distillation Unit Vacuum Distillation Unit Vacuum Residue Diluent Recycled Bitumen Diluent Vacuum Gas Oil to Refinery LVGO HVGO off gases A Typical Bitumen Upgrader

A Simplified Refinery Flow Diagram LSR H/T Penex LPG, C3= Hydrogen Catalytic Reformer NHT Atm Unit Gasoline Blending Crude Oil FCCU DHT Distillate Fuels Vac Unit H/C GDU Coker Unit Coke Asphalt

Crack Spread Declining

2009 Market Indicators Are Lower 2008 2Q 2009 2Q Chicago LLS 6-3-2-1($/BBL) 2.71 5.73 Sweet/Sour Diff., ($/BBL) 13.74 3.98 NYMEX WTI ($/BBL) 123.80 59.80

US Refiners Produce Low Sulfur Gasoline 2006 gasoline sulfur regulation of < 30 wppm S US refiners met regulation using a variety of technologies and hydrotreating catalysts Optimized gasoline desulfurization to preserve octane Technologies used included Axens Prime G CD Tech ConocoPhillips Szorb ExxonMobil Scanfining Pool gasoline octane losses of 1 to 3 numbers

Ethanol Blending & Naphtha Reforming US goal is 35 billion gallons per year of ethanol in gasoline by 2022 E10 gasoline lead to Increased gasoline volume Gasoline octane giveaway Low severity reformer operations Lower hydrogen production Inefficient catalytic reformer productivity Maximize gasoline octane barrels and hydrogen Energy savings negligible relative to losses of H2 and reformate Key benefits are less utilization of crude oil for gasoline and enhanced environmental quality

US EPA Gasoline Benzene Regulation US EPA Mobile Source Air Toxics II (MSAT II) regulations effective Jan 2011 Annual corporate average gasoline pool benzene of 0.62 vol. % Credits and trade arrangements possible By July 2012, maximum refinery average gasoline benzene of 1.3 vol. % Catalytic Reformers produce over 80 % of gasoline benzene Naphtha Pre-fractionation and Post-fractionation Pre-fractionation employs naphtha split to reduce benzene and precursors to the reformer Naphtha Splitter at the crude unit or after NHT Benzene and precursors converted via Bensat and C5/C6 isomerization Achieved ~ 35 to 50 % drop in gasoline benzene at two Marathon refineries Gasoline benzene credits option

US EPA Gasoline Benzene Regulation Post-fractionation and gasoline benzene minimization processes Extractive distillation for benzene UOP, Uhde Reduced gasoline volume Octane impact Benzene saturation Axens, UOP Gasoline volume maintained Impact on Octane & H2 consumption Benzene alkylation to cumene Capital intensive processes for reducing gasoline benzene and maximizing hydrogen production

N. American Clean Diesel Growth Through 2018 Source: Hart World Refining & Fuels Service 17 17

Oil Refiners Met ULSD Regulation Technology and oil refining companies honed in on refractory sulfur compounds including 4,6 DM DBT Utilized a combination of new hydrotreating catalysts, increased reactor volumes, reactor internals process modifications Grassroots Units (~15%) Unit Revamps (~75%) No modifications (~10%) Oil refiners achieved < 10 wppm sulfur to meet pipeline requirements S H3C CH3

Renewable Diesel Fuels Information The mandate for annual renewable fuels use is 36 billion gallons of biofuels by 2022 Biodiesel is a renewable fuel for diesel engines from natural oils -- soybean oil via reaction with methanol comprised of mono-alkyl esters of long fatty acids meets specifications of ASTM D67511 pure biodiesel is B100 Biodiesel blend is a blend of biodiesel fuel with petroleum based diesel fuel BXX, where XX represents percentage of biodiesel B2, B5 and B20 are used Ref: Biodiesel Technical Information, ADM Biodiesel Technical Services

US Biodiesel Production On the Rise B20 emissions are lower than conventional diesel 21 % lower HCs 11 % lower CO 20 % lower PMs ~ 5 % + NOx 20 % lower PAH Ref: Clean Cities Fact Sheet US DOE Apr. 2008

Biofuels Use Will Increase Substantially Source: Hart World Refining & Fuels Service % of Fuel Supply Biofuels demand in US which is mainly ethanol is expected to grow from just around 8% today (which is really nothing more than replacement of MTBE) to just around 10% of entire US gasoline pool by 2025. Biofuels Demand in Latin America, which mainly is Brazil (both ethanol and biodiesel (from soy)) is expected to grow from just above 8% to just below 14% of US gasoline demand. Biodiesel demand in Europe is expected the highest increase from 1% in 2006 to over 10 in 2025…… that said, their targets for 2007 was much higher than they achieved. 21 21

Summary Unconventional oils will have a significant impact on US refining plants reliability and profitability Cost of meeting environmental regulations and GHG re bitumen production will be a factor Ethanol gasoline and benzene will challenge US refiners Diesel growth is expected worldwide relative to gasoline Biofuels use would increase significantly in the next 15 years

The Future -- Gas to Liquids ?

Upgraded Bitumen Still Challenging Oil Type Arab Med(1) Maya WCS(4) Athabasca Bitumen(3) Muskeg R. Bitumen(3) Gravity, API 30.7 20.9 19.7 7.5 11.2 Sulfur, wt. % 2.4 3.4 3.2 4.8 4.6 TAN, mg/g 0.25 0.32 1.0 3.5 2.9 Ni, wppm 4 52 150 58 V, wppm 18 232 122 290 151 Marathon crude oil assay database V/Ni ratio a parameter for palaeo-environmental characteristics…., F. Galarraga, et.al., J. Petro. Science, 61, Issue 1, pages 9-14, April 2008 Tutorial on upgrading oil sands bitumen, M. R. Gray, University of Alberta. WCS is Western Canadian Select