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IH2 Technology: Bagasse to Hydrocarbon Fuels
Pat Leung
CRI Catalyst Company
Disclaimer
This presentation contains forward-looking statements concerning the financial condition, results of operations...
• The IH2 technology, invented by Gas Technology Institute,
produces high quality hydrocarbon fuels and blend stock direct...
Main Points
• What is IH2 Technology?
• Bagasse as Feedstock
• Integration of IH2 Plant with Sugar
Production
• Commercial...
5
2) Fluidized Bed
Proprietary
Catalyst System
Renewable H2
340-470C
<500psig
1) Feed Conditioning
Sizing , Drying & Feedi...
What is IH2 Technology?
Wood
(Hard-Soft)
Lemna MicroAlgae Bagasse MacroAlgae Corn Stover
Feed wt % C 49.7 46.3 43.1 43.1 3...
Bagasse as Feedstock
Wood
(Hard-Soft)
Lemna MicroAlgae Bagasse MacroAlgae Corn Stover
Feed wt % C 49.7 46.3 43.1 43.1 34.0...
• Available at mill in large quantities
• Bagasse is not edible
• Produces high quality hydrocarbon fuel
• Synergy of a su...
Integration
IH2 UnitBagasse
Cane Trash/
Sugar Cane Tops
Sugar
Cane
Sugar
Factory
Enhanced
Energy
Integration
Hot water
HP ...
• Bench Scale
– Since 02/2009 @ 0.5kg/hr
• Pilot Scale
– Since 02/2012 @ 50kg/d
– Confirmed bench scale results
– Producin...
4.7
17.7
4.0
55.0
2.8
2.8
40.5
Feed
1st Stage/2nd Stage
Fractionation
HMU
Ammonium Sulfate
Absorption/Stripping
Installed ...
• The IH2 technology produces high quality hydrocarbon fuels and
blend stock directly from biomass
• Feedstock flexible wi...
Thank You
13
Learn more at
http://www.cricatalyst.com/catalysts/renewables.html
http://www.gastechnology.org/Solutions/Pag...
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WBM Brazil IH2 Presentation

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  1. 1. IH2 Technology: Bagasse to Hydrocarbon Fuels Pat Leung CRI Catalyst Company
  2. 2. Disclaimer This presentation contains forward-looking statements concerning the financial condition, results of operations and businesses of Royal Dutch Shell. All statements other than statements of historical fact are, or may be deemed to be, forward-looking statements. Forward- looking statements are statements of future expectations that are based on management’s current expectations and assumptions and involve known and unknown risks and uncertainties that could cause actual results, performance or events to differ materially from those expressed or implied in these statements. Forward-looking statements include, among other things, statements concerning the potential exposure of Royal Dutch Shell to market risks and statements expressing management’s expectations, beliefs, estimates, forecasts, projections and assumptions. These forward-looking statements are identified by their use of terms and phrases such as ‘‘anticipate’’, ‘‘believe’’, ‘‘could’’, ‘‘estimate’’, ‘‘expect’’, ‘‘goals’’, ‘‘intend’’, ‘‘may’’, ‘‘objectives’’, ‘‘outlook’’, ‘‘plan’’, ‘‘probably’’, ‘‘project’’, ‘‘risks’’, ‘‘seek’’, ‘‘should’’, ‘‘target’’, ‘‘will’’ and similar terms and phrases. There are a number of factors that could affect the future operations of Royal Dutch Shell and could cause those results to differ materially from those expressed in the forward-looking statements included in this presentation, including (without limitation): (a) price fluctuations in crude oil and natural gas; (b) changes in demand for Shell’s products; (c) currency fluctuations; (d) drilling and production results; (e) reserves estimates; (f) loss of market share and industry competition; (g) environmental and physical risks; (h) risks associated with the identification of suitable potential acquisition properties and targets, and successful negotiation and completion of such transactions; (i) the risk of doing business in developing countries and countries subject to international sanctions; (j) legislative, fiscal and regulatory developments including regulatory measures addressing climate change; (k) economic and financial market conditions in various countries and regions; (l) political risks, including the risks of expropriation and renegotiation of the terms of contracts with governmental entities, delays or advancements in the approval of projects and delays in the reimbursement for shared costs; and (m) changes in trading conditions. All forward-looking statements contained in this presentation are expressly qualified in their entirety by the cautionary statements contained or referred to in this section. Readers should not place undue reliance on forward-looking statements. Additional factors that may affect future results are contained in Royal Dutch Shell’s 20-F for the year ended December 31, 2012 (available at www.shell.com/investor and www.sec.gov ). These factors also should be considered by the reader. Each forward-looking statement speaks only as of the date of this presentation, 17 September 2013 Neither Royal Dutch Shell nor any of its subsidiaries undertake any obligation to publicly update or revise any forward-looking statement as a result of new information, future events or other information. In light of these risks, results could differ materially from those stated, implied or inferred from the forward-looking statements contained in this presentation.
  3. 3. • The IH2 technology, invented by Gas Technology Institute, produces high quality hydrocarbon fuels and blend stock directly from biomass • Feedstock flexible with high product yields • Bagasse converts at 100 gallons per US ton raising the possibility of integrating an IH2 unit with a Brazilian cane sugar mill • Nearly carbon neutral* • Attractive economics *>94% GHG reduction per Professor David Shonnard at MTU: http://services.lib.mtu.edu/etd/THESIS/2012/ChemicalEng/maleche/thesis.pdf Executive Summary
  4. 4. Main Points • What is IH2 Technology? • Bagasse as Feedstock • Integration of IH2 Plant with Sugar Production • Commercial Status • Attractive Economics
  5. 5. 5 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 GasRenewable H2 Process Gasoline, Jet and Diesel Hydrocarbons (67-172 gal/ton) R100 Regular Gasoline (Wood) R100 Intermediate Gasoline (Wood) R60 + Diesel (Wood) Products Distilled Hydrocarbon Hi Pressure Steam Clean Water Fertilizer BioChar Biogenic CO2 City Waste Wood/Forest Residue Energy Crops Algae Feed 5) Cyclones What is IH2 Technology? Crop Residue
  6. 6. What is IH2 Technology? Wood (Hard-Soft) Lemna MicroAlgae Bagasse MacroAlgae Corn Stover Feed wt % C 49.7 46.3 43.1 43.1 34.0 40.2 Feed wt % H 5.8 5.8 6.1 5.0 4.43 5.0 Feed wt % O 43.9 35.7 20.4 35.3 23.6 35.7 Feed wt % N 0.11 3.7 6.5 0.34 4.6 1.0 Feed wt % S 0.03 0.3 0.7 0.10 1.9 0.05 Feed wt % Ash 0.5 8.2 23.1 16.2 29.4 18.1 Feed H/C 1.40 1.50 1.70 1.39 1.56 1.49 Typical % C4 + Liquid Yield (MAF) (Moisture/Ash Free) 26-30 30 46 30 35 21 C4+ Gallon/Ton (MAF) 86-92 100 157 100 119 67 Product Oxygen b d l b d l b d l b d l b d l b d l Product TAN# <0.02* <0.05 <0.05 <0.05 <0.05 <0.05
  7. 7. Bagasse as Feedstock Wood (Hard-Soft) Lemna MicroAlgae Bagasse MacroAlgae Corn Stover Feed wt % C 49.7 46.3 43.1 43.1 34.0 40.2 Feed wt % H 5.8 5.8 6.1 5.0 4.43 5.0 Feed wt % O 43.9 35.7 20.4 35.3 23.6 35.7 Feed wt % N 0.11 3.7 6.5 0.34 4.6 1.0 Feed wt % S 0.03 0.3 0.7 0.10 1.9 0.05 Feed wt % Ash 0.5 8.2 23.1 16.2 29.4 18.1 Feed H/C 1.40 1.50 1.70 1.39 1.56 1.49 Typical % C4 + Liquid Yield (MAF) (Moisture/Ash Free) 26-30 30 46 30 35 21 C4+ Gallon/Ton (MAF) 86-92 100 157 100 119 67 Product Oxygen b d l b d l b d l b d l b d l b d l Product TAN# <0.02* <0.05 <0.05 <0.05 <0.05 <0.05
  8. 8. • Available at mill in large quantities • Bagasse is not edible • Produces high quality hydrocarbon fuel • Synergy of a sugar mill with a bagasse-fed IH2 plant - Export steam - Low value heat - Export electricity • Available in countries with growing energy demands • Bagasse is currently used for power and LP steam generation Bagasse as Feedstock
  9. 9. Integration IH2 UnitBagasse Cane Trash/ Sugar Cane Tops Sugar Cane Sugar Factory Enhanced Energy Integration Hot water HP SteamCo-Gen Sale to grid Sugar Molasses Fuels Boiler Char LP Steam
  10. 10. • Bench Scale – Since 02/2009 @ 0.5kg/hr • Pilot Scale – Since 02/2012 @ 50kg/d – Confirmed bench scale results – Producing fuels for EPA Registration – Producing fuels for EN Qualification • Pre Commercial Scale – BDEP for 5mt/d cellulose done – 2 showcase licenses awarded since 12/2012 • Commercial Scale – KBR is CRI’s exclusive commercial engineering partner – 500 & 1000mt/d stand alone USGC wood FEL-2 completed; FEL-3 begins – 2 commercial licenses awarded since 06/2013 109/16/2013 Commercial Status
  11. 11. 4.7 17.7 4.0 55.0 2.8 2.8 40.5 Feed 1st Stage/2nd Stage Fractionation HMU Ammonium Sulfate Absorption/Stripping Installed Equipment Costs $127.5MM • Stand Alone/Green Field (US Gulf Coast basis) • 2000mt/d wood at 10% moisture • TIC of $127.5MM results in TCI of $263MM • HMU (SMR) is largest single expense @ $55mln ~45% TIC • Feed Stock ~55% of Operating Cost • No subsidies, tax credits included! $3.96capex/annual gallon • KBR FEED underway (FEL-2 complete) • Opex validated by prospective clients • Minimum Fuel Selling Price: $0.433/L (2007) $0.476/L (2012) $1.64/gal $1.80/gal • Refinery Synergy w/Refinery H2 Supply - Estimated MFSP $0.359/L (2007) $0.394/L (2012) $1.36/gal $1.49/gal 9/16/2013 11 91.31 7.8 2.14 17.3 5.9 29.6 Wood $71.97/dry ton Other Op Costs: Catalyst, Disposal, etc. Fixed Cost Depreciation Avg Income Tax Avg ROI Operating Costs Total $1.64/gal* *Includes $0.1884/gal coproduct credit http://www.osti.gov/bridge/servlets/purl/1059031/1059031.pdf Attractive Economics
  12. 12. • The IH2 technology produces high quality hydrocarbon fuels and blend stock directly from biomass • Feedstock flexible with high product yields • Presents an opportunity for bagasse / cane mill integration worthy of further study • Nearly carbon neutral* • Attractive economics • Available exclusively from CRI *>94% GHG reduction per Professor David Shonnard at MTU: http://services.lib.mtu.edu/etd/THESIS/2012/ChemicalEng/maleche/thesis.pdf Conclusion
  13. 13. Thank You 13 Learn more at http://www.cricatalyst.com/catalysts/renewables.html http://www.gastechnology.org/Solutions/Pages/default.aspx
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