The document is a presentation about IH2 technology for producing renewable fuels from biomass. It discusses how the technology can integrate with existing refinery and agricultural assets to produce drop-in gasoline, diesel, and jet fuels. It provides an overview of the commercialization process from early lab demonstrations through current pilot plants. Product quality is shown to be improving over generations of catalyst development and now meets fuel standards. Economics are estimated to be attractive at less than $2.25 per gallon.

1. IH2 Technology: Integration With Existing Assets
Pat Leung, CRI Catalyst Company, 910 Louisiana, Houston, TX 77002
RENEW. REFINE. REFUEL.
ARTC Presentation
6 March 2014

2. Disclaimer
This presentation contains forward-looking statements concerning the financial condition, results of operations and businesses
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4/10/2014 2

3. Main Points
• Why IH2 technology?
• Integration with existing assets
• Commercialization Process
• Product Quality Update
• Executive Summary
4/10/2014 3

4. Why IH2 Technology?
4/10/2014 4
• Self-sufficient, self-contained and self-sustaining
• Feedstock flexible, product yields 67-172 gal/ton (MAF)
 Spans gasoline, jet and diesel range
 No detectable oxygen or TAN
• High GHG reductions
• Integrates commercially proven equipment; Market Ready
• Attractive economics (< $2.25/gal; 2000 dry mt wood/day USGC pricing)
 $450mln TCI ex KBR; 60% financed @ 8%; 20% overall IRR; $72/dry ton feed
 No RINs, No Carbon or Blending Credits, No Subsidies of any kind included
• Improved catalysts  enhanced product yield & quality

5. 4/10/2014 5
Distilled
Hydrocarbon
Hi Pressure
Steam
Clean Water
Fertilizer
BioChar
Biogenic CO2
Crop Residue
City Waste
Wood/Forest
Residue
Energy Crops
Algae
Gasoline, Jet and Diesel
Hydrocarbons (67‐172 gal/ton)
R100 Regular Gasoline (Wood)
R100 Intermediate Gasoline (Wood)
R100 Diesel (Wood)
Feed
Products
2) Fluidized Bed
Proprietary
Catalyst System
Renewable H2
340‐470C
<500psig
1) Feed Conditioning
Sizing , Drying & Feeding
1st Stage 2nd Stage
3) Fixed Bed
Proprietary
Catalyst System
Renewable H2
<500psig
4) SMR C1‐C3 Gas
Renewable H2
Process
5) Cyclones
Why IH2 Technology?

6. 4/10/2014 6
Option 1: Full Standalone
Location Flexibility, Minimum Environmental Impact
Maximum GHG reduction
Lowest CI product
Highest Capital Cost
Option 2: Integrated with Refinery HT
Minimum Environmental Impact
Lowest CI product
Maximum GHG reduction
Lower Capital Cost
Option 3 Integrated with Refinery H2
Higher Environmental Impact
Reduced GHG reduction
Higher CI product
Lowest Cost
Capital 20% - 25% lower than base case
Integration with Existing Assets - Refinery

7. 4/10/2014 7
Integration with Existing Assets - Sugar Mill
IH2 UnitBagasse
Cane Trash/
Sugar Cane Tops
Sugar
Cane
Sugar
Factory
Enhanced
Energy
Integration
Hot water
HP
Steam
Co-Gen
Sale to grid
Sugar
Molasses
Fuels
Boiler
Char
LP Steam

8. 4/10/2014 8
Growth Harvest Extraction
Primary Product(s)
Residues
NH3 / S
LP Steam / Hot Water
CO2
HP Steam or HP Steam to Power
Fuel
100 gal/ton MAF
70% gasoline/
30% diesel
Integration with Existing Assets - Algae Facility

9. 4/10/2014 9
Growth Harvest Extraction
Whole Algae
NH3 / S
LP Steam / Hot Water
CO2
HP Steam or HP Steam to Power
Fuel
157 -172 gal/ton MAF
(50% gasoline/
50% diesel)
Integration with Existing Assets - Algae Facility

10. 4/10/2014 10
0.02L/day
Bangalore 1L/day
Chicago, Bangalore
22L/day
Chicago
2000L/day
NanoScale EE HT tools
GTI/CRI Design Basis
Commercially Engineered
Commercially Fabricated
1st Stage System
2nd Stage System
On line analytical suite
Up to 16 runs/day/system
Chicago Unit
GTI Design Basis
GTI Built
Bangalore Unit
GTI/CRI Design Basis
Commercially Engineered
Commercially Fabricated
Mixture online/offline
Up to 3 runs/week
GTI Design Basis
Commercially Engineered
Commercially Fabricated
Mixture Online/Offline
Up to 1 run/week
GTI/CRI Design Basis
Commercially Engineered
Mixture Online/Offline
Up to 3 runs/month
Commercialization Process

11. 2009
2010
2011
2012
2013
2014
2015
2009
2010
2011
2012
2013
2014
2015
GTI first demonstrates IH2 technology at MBU (bench) scale March
1st gen CRI catalysts developed June
GTI executes Joint Development and exclusive Commercial Agreements with CRI
2nd gen CRI catalysts developed April
GTI demonstrates process flexibility & product yields MBU scale
CRI executes ESAs with Zeton and KBR
GTI IH2® 50kg/day pilot plant commissioned February
3rd gen CRI catalysts developed August
1st demo license executed December
KBR finalizes customer site-specific FEL-2 September
CRI Nanoflow 2nd stage & MBU commissioned
2 commercial and 1 demo license executed June-August
GTI’s first Patent issued
CRI Nanoflow 1st stage commissioned
Expect more customer FEL-2 / 3 studies
4th gen CRI catalysts developed January
First LCAs published
4/10/2014 11
Commercialization Process

12. 4/10/2014 12
Commercialization Process - 3D Rendering

13. 4/10/2014 13
Hydrocarbon
Water
Total Liquid Product
2nd Gen Catalysts Lab Scale
Total Liquid Product
1st Gen Catalysts Lab Scale
Hydrocarbon
Water
Gas/Jet/Diesel Product
3rd Gen Catalysts Lab Scale
4Q09 “R5” 3Q10 “R25” 2Q12 “R60+”
Improve product yield, appearance and quality
Product Quality Update
Jet/Diesel Product
4th Gen Catalysts Lab Scale
1Q14 “R100”

14. 144/10/2014
Product Quality Update
Gasoline Product
3rd Gen Catalyst
Pilot Plant Scale
Drop In / Tank Ready
R100 Quality
Jet/Diesel Product
3rd Gen Catalyst
Pilot Plant Scale
> R60 Quality
Water Product
3rd Gen Catalyst
Pilot Plant Scale
Clean, No Carbon

15. Product Quality Update
4/10/2014 15
US
• Gasoline (from wood):
 R100 Meets ASTM D-4814-10b
 ~87 Octane
 S < 15-ppm
• Diesel (from wood)
 Approaching R100
 ASTM D-975-11
 Derived Cetane # approx. 40
 S < 10-ppm
Europe:
• Petrol (from wood)
 Petrol (from wood)
 EN 228: Petrol – Jan 2009
 Octane Low
 S ~10-ppm
• Diesel (from wood)
 EN 590:2009+A1:2010
 Cetane # Low
 S ~15-ppm
• 3rd Party Testing in Progress in 2014
• More Upgrading Wood Product for
EU Specs

16. Executive Summary
4/10/2014 16
• Self-sufficient, self-contained and self-sustaining
• Feedstock flexible, product yields 67-172 gal/ton (MAF)
 Spans gasoline, jet and diesel range
 No detectable oxygen or TAN
• High GHG reductions
• Integrates commercially proven equipment; Market Ready
• Attractive economics (< $2.25/gal; 2000 dry mt wood/day USGC pricing)
• Improved catalysts  enhanced product yield & quality
• Available exclusively from CRI Catalyst Company

17. Thank You
4/10/2014 17
Learn more at
http://www.cricatalyst.com/catalysts/renewables.html