Syn Gasifier ALTERNATIVE ENERGY Technology Presentation COAL GASIFICATION

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Syn. Gasifier ALTERNATIVE ENERGY Technology Presentation

Syn. Gasifier ALTERNATIVE ENERGY Technology Presentation

COAL GASIFICATION versus COAL COMBUSTION

COAL GASIFICATION versus COAL COMBUSTION

Basic Gasification Technology • Dry Feed Entrained Flow Gasifier using: – Pyrolysis – Thermal

Basic Gasification Technology • Dry Feed Entrained Flow Gasifier using: – Pyrolysis – Thermal conversion or destruction of organics in the absence of oxygen (reducing atmosphere). – Gasification – Thermal conversion of organic materials at elevated temperatures and reducing conditions to produce syngas (Hydrogen and Carbon Monoxide) – Steam Reformation – Vaporized water (steam) added to carbon creates syngas (Hydrogen and Carbon Monoxide)

From: NREL: Biomass Gasification Overview, Richard L. Bain, January 28, 2004

From: NREL: Biomass Gasification Overview, Richard L. Bain, January 28, 2004

Provisional Patent Effective Date: April 11, 2006 Patent Pending Effective Date:

Provisional Patent Effective Date: April 11, 2006 Patent Pending Effective Date:

Exclusive Patent Rights Assigned To Thermal Conversions, LLC

Exclusive Patent Rights Assigned To Thermal Conversions, LLC

175 dry ton per day Gasification Plant

175 dry ton per day Gasification Plant

www. eastman. com/company/gasification/overview. htm

www. eastman. com/company/gasification/overview. htm

Coal Syngas 12, 500 BTU Variable gas compositions available depending upon operation parameters Heat

Coal Syngas 12, 500 BTU Variable gas compositions available depending upon operation parameters Heat up to 1800° F Pressure 80 psi • • • Carbon Dioxide Carbon Monoxide Hydrogen Methane Other • Ash Plus Ionized Water Injection Gasification – – – Sulfur Silica Mercury Chlorine Sodium, etc Feed for Chemical/ Refinery Processes and Electrical Generation Removed

Energy Mass Balance (Btu Basis)

Energy Mass Balance (Btu Basis)

Syngas composition operating range for pyrolysis/steam reforming system which includes the range of H

Syngas composition operating range for pyrolysis/steam reforming system which includes the range of H 2: CO most desirable for production of synthesis fuels. Data collected on pilot scale pyrolysis/steam reforming system operated on biomass feedstock. (Schuetzle, et al. 2007)

Gasification Chemistry • The following chemical equations describe the process that takes place in

Gasification Chemistry • The following chemical equations describe the process that takes place in the conversion of coal or other carbonaceous fuels into synthesis gas.

Process Equations Combustion with Oxygen: C + O 2 ↔ CO 2 Gasification with

Process Equations Combustion with Oxygen: C + O 2 ↔ CO 2 Gasification with Oxygen: 2 C + O 2 ↔ 2 CO Gasification with Carbon Dioxide: C + CO 2 ↔ 2 CO Gasification with Steam: C + H 2 O ↔ CO + H 2 Gasification with Hydrogen: C + 2 H 2 ↔ CH 4 Water Gas Shift Reaction: CO + H 2 O ↔ H 2 + CO 2 Methanation Reaction: CO + 3 H 2 ↔ CH 4 + H 2 O

Syn. Gasifier Unique Equations NOx Emission Control: CO + NOx +H 2 O ↔

Syn. Gasifier Unique Equations NOx Emission Control: CO + NOx +H 2 O ↔ O 2 CNO + H 2 O 2 Reaction creates Nitroxyl reactive ions and hydrogen peroxide vapor which provides additional quench water purification and final Nitroxyl precipitation into water filters.

Syn. Gasifier Unique Equations Continued Sulfur Emission Control: CO + SOx +H 2 O

Syn. Gasifier Unique Equations Continued Sulfur Emission Control: CO + SOx +H 2 O ↔ O 2 CSO + H 2 O 2 Reaction creates Sulfinoxyl reactive ions and hydrogen peroxide vapor which provides additional quench water purification and final Sulfinoxyl precipitation into water filters.

Syn. Gasifier Unique Equations Continued Metals Emission Control: O-x + M ↔ MOx Ionized

Syn. Gasifier Unique Equations Continued Metals Emission Control: O-x + M ↔ MOx Ionized oxygen reaction creates metal oxides which are coagulated and precipitated into water filters.

Major US Gasification System Vendors and Projects • E-GAS Conoco. Phillips – Upflow, wet

Major US Gasification System Vendors and Projects • E-GAS Conoco. Phillips – Upflow, wet fed (slurry) • GE Energy – Downflow, wet fed (slurry) • Shell Gasification – Upflow, dry fed • All use an entrained flow oxygen-blown system of gasification • Conoco. Phillips (Global Energy/PSI Wabash River) and GE Energy (Tampa Electric Polk Station) have demonstrated and proven technology in commercial scale IGCC plants

Comparison with Major Entrained Flow Gasifiers Technology Name/ Design Feature GE Energy (formerly Texaco)

Comparison with Major Entrained Flow Gasifiers Technology Name/ Design Feature GE Energy (formerly Texaco) E-Gas (Conoco. Phillips) Shell Syn. Gasifier Feed System Coal in Water Slurry Dry coal, Lock Hopper & Pneumatic Conveying Dry (As Received) Coal, Air lock Drag Conveyor Gasifier Configuration Single Stage Downflow Two Stage Upflow Single Stage Upflow 4 Stage Horizontal Circular Flow Gasifier Wall Refractory Membrane Wall Inconel Pressure (psig) 500 -1000 Up to 600 80 Notes Offered as Quench or with Heat Recovery Currently only offered with Heat Recovery Quench Only Reference: Publication No. LFEE 2005 -002 WP MIT Laboratory for Energy and the Environment

Fischer Tropsch Liquid Fuels Process

Fischer Tropsch Liquid Fuels Process

The Fischer Tropsch Process

The Fischer Tropsch Process

Tax Credits • Syn. Gas gasification projects can qualify for several tax credits: –

Tax Credits • Syn. Gas gasification projects can qualify for several tax credits: – Investment tax credits – Clean coal technology – Alternative fuels – Bio-mass conversion – Waste conversion – Job creation

PC Emissions Improvements

PC Emissions Improvements

IGCC Power Plant Mass Flow

IGCC Power Plant Mass Flow

Power Plant Efficiency is defined as the amount of electrical energy produced for sale

Power Plant Efficiency is defined as the amount of electrical energy produced for sale as a fraction of the amount of fuel consumed in the process, expressed as a percentage. • • • Conventional – 32 to 37 % Supercritical – 35 to 43 % Ultra-supercritical – 45 % potential Circulating Fluidized Bed – 29 to 34 % IGCC (Integrated Gasification Combined Cycle) – 37 to 43 % with potential of 50 %

Electricity Flow, 2005 (Quadrillion Btu) 65. 1% 34. 9% 31. 3% http: //www. eia.

Electricity Flow, 2005 (Quadrillion Btu) 65. 1% 34. 9% 31. 3% http: //www. eia. doe. gov/emeu/aer/contents. html

Efficiency in Electricity Generation by Process www. umweltbundesamt. at/. . . /site/umweltthemen/industrie/IPPC_Konferenz/donnerstag_kraftwerke/6 -_Van_Aart. ppt

Efficiency in Electricity Generation by Process www. umweltbundesamt. at/. . . /site/umweltthemen/industrie/IPPC_Konferenz/donnerstag_kraftwerke/6 -_Van_Aart. ppt

Greenhouse Gas Emissions

Greenhouse Gas Emissions

CO 2 Emission Sources

CO 2 Emission Sources

Bio. Mass Syn. Gas Flame

Bio. Mass Syn. Gas Flame