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Abstract A large share of the agricultural biomass resource remains underutilized while local and national policies continue to mandate increasing levels of renewable energy. Only a small fraction of the available agricultural residues are currently utilized for energy, even where sustainability would support it. This virtually untapped resource for energy has struggled because it is low in energy density, diffusely located, and costly to transport to large, centralized energy facilities. The use of smaller on-site gasification systems to produce bio-syngas from agricultural biomass residues shows promise for increasing resource utilization for displacement of fossil fuels. Bio-syngas generated in on-site systems can provide a direct energy substitution for natural gas in gas devices like boilers, dryers, heaters, engines, etc. Proliferation of these systems would help industrial and agricultural processing facilities trying to decrease their carbon emissions footprint, a large part of which comes from on-site natural gas usage. This project shows the technical, economic, and environmental feasibilities associated with on-site conversion of residue biomass to bio-syngas for fuel in industrial and agricultural applications. The project samples and characterizes the physical, chemical, and thermal properties of the biomass residues and resulting bio-syngas from the CircleDraft® gasifier system being deployed for commercial operation by West Biofuels, LLC, and its development partner, INSER Energia, S.P.A. The project develops the optimal feedstock and operational conditions required to deliver bio-syngas that is compatible with common natural-gas devices used in industry. In addition, the market potential of the bio- char produced as a byproduct of the gasification process is reviewed. The optimized results are used to evaluate the overall costs of using bio-syngas in comparison with current and forecast industrial natural-gas prices, to determine the economic feasibility for commercial projects. The net environmental benefits including potential greenhouse gas emission reductions and carbon sequestration will be reviewed. Project Goal: The goal of this project is to determine the feasibility of using currently underutilized agricultural biomass residues for conversion to synthetic gas to replace or blend with natural gas for direct, on-site industrial and agricultural use References Faussone, G.C. 2012. Biomass Gasification With CircleDraft Process. Published online in Wiley Online Library (wileyonlinelibrary.com). DOI 10.1002/ep.11608 Faussone, G.C. 2014. Personal Communication. Tittmann, P., N. Parker, Q. Hart and B. Jenkins. 2008. Economic potential of California biomass resources for energy and biofuel. PIER Collaborative Report, California Energy Commission, Sacramento, CA. U.S. Energy Information Administration (EIA). 2014. California Natural Gas Statistics. http://www.eia.gov/dnav/ng/hist/n3035ca2A.htm USDA NASS. 2013. California Field Crop Review 34(2), 21 February, www.nass.usda.gov/ca. Williams, R.B., et al. 2008. An Assessment of Biomass Resources in California, 2007. PIER Collaborative Report, California Energy Commission, Sacramento, CA. Conclusion An 2-MW thermal biomass gas production facility has been constructed and is being operated in California for demonstration on both forest and agricultural biomass feedstock. The produced gas is intended to be used as a replacement for natural gas in typical gas appliances used by the processing industries. While the project is ongoing, early results indicate that the performance targets listed above are within the capabilities of the technology. Acknowledgement: Funds for this project were provided by West Biofuels and the California Energy Commission under Grant Agreement Number: #14-01-11G ON-SITE BIOMASS GASIFICATION AS A NATURAL GAS SUBSTITUTE Dr. Matthew Summers, Dr. Chang-hsien Liao, Mr. Matthew Hart, West Biofuels LLC, Woodland, CA 95776 USA Dr. Gian Claudio Faussone, INSER Energia S.p.A., C.so Appio Claudio, 229/5, Torino 10146 ITALY Dr. Reinhard Seiser, Dr. Robert Cattolica, University of California at San Diego, La Jolla, CA 92093 USA Project Tasks Performance / Cost Objectives 1) Experimental design and selection and characterization of available biomass residues from agricultural sector At least 3 specific biomass residues will be selected for potential suitability for gasification via the CircleDraft ® gasifier system that meet criteria for high-quality gasification. The experimental design will be developed to determine the performance and the gas quality from each feedstock at various operating conditions. Performance targets: Statewide Availability: 1 million tons/year aggregate; Cost: < $30 per ton; Moisture Content: < 25%; Ash Content: < 5%; Higher Heating Value: > 7,000 BTU/lb; Ash Melting Temperature: >1100°C; Particle Size: < 3 in. 2) Setup measurement systems to characterize performance and gas quality on a commercial CircleDraft ® gasifier system A CircleDraft ® gasifier system will be provided by West Biofuels that nominally produces 6.75 MMBTU/hr of synthetic gas from 1000 pounds per hour of dry wood chips and will be outfitted with sensors and sampling ports so that the performance and gas quality can be analyzed for the selected residue feedstock. Performance targets: Feedstock: mass flow measurement to ± 5% and composition to ± 3%; Gas: flow measurement to ± 10% and characterize 99% of major and trace gases; Energy: heating value to ± 3% for feedstock and synthetic gas. 3) Conduct testing of biomass feedstock for performance and gas quality with CircleDraft ® gasifier system Tests with each feedstock will be conducted with the CircleDraft ® gasifier system over a range of selected operating conditions from the experimental design and the performance of the gasifier will be measured and the gas quality characterized. Performance targets: Gasifier efficiency: >70%; Gas heating value: 150- 300 BTU/SCF; Gas inert content: <60%; Gas impurities: Less than air quality and manufacturer requirements; 4) Analysis of technical and economic feasibility of natural gas replacement Based on the optimal results from Task 3, the technical and economic feasibility of industrial or agricultural on-site gasifier projects for the replacement of natural gas will be developed. Performance targets: Compatibility with natural gas devices (boilers/engines); Gasifier system capital cost: <$100,000 per MMBTU/hr capacity; Operating hours: 7000/year; Synthetic gas cost: $6-$12/MMBTU; Project simple payback: 3-6 years; Agricultural Biomass Potential Type Current Industry Energy Usage BCHP Energy Production Potential* Net Energy Potential Power (GWh) 744 1366 622 Power Value ($) -$120 M @ $0.16/kWh $188 M $68M @ $0.11/kWh Natural Gas (BCF) 14.9 49 34.1 Nat Gas Value ($) -$119 M @ $8/1000 ft 3 $255 M $136 M @ $4/1000 ft 3 * From Estimated 825,000 BDT of almond shell and 750,000 BDT of prunings. California Biomass Feedstock Potential California Almond Industry Energy Potential vs. Current Usage Almond Shell Almond Pruning The CircleDraft® Gasification Process CircleDraft® Gasifier Process Unit Specifications Description Value Fuel Type Chips, Shells, Residue Pellets & Cubes Oxidant Humidified Air Fuel Heating Value 8,500 BTU/dry lb Moisture 25% Specific Consumption 150 lbs/MMBTU Gas Production Rate 45 SCF/dry lb Gas Heating Value 150 BTU/SCF Fuel Consumption ~ 1000 lbs/hr Total Gas Output 6.75 MMBTU/hr Electrical Consumption 90 kW Working Temperatures 350 °C -1050 °C Pressure Max: 20 in H2O Thermal Efficiency 75% Erection of Gasifier Structure Fabrication of Lower Grate Housing Upper Reactor with Feeder Lower Cone Hot Face Refractory Lower Cone Prior to Grate Installation Modular Control Room Fabrication Plant Construction Synthetic Gas Characteristic CircleDraft® Range H 2 10 - 35% CO 15 - 48% CH 4 1 - 4% C 2 H 4 0.1 - 0.5% C 3 + 0.1 - 0.3% CO 2 0.1 – 15% N 2 15 - 49% H 2 /CO Ratio 0.5 – 1.5 HHV (MJ/Nm 3 ) [BTU/scf] 5.6 – 10.3 [150 - 300] Wobbe Index (MJ/Nm 3 ) 22 – 38 Tars (mg/Nm 3 ) 5 - 25 Particulate (mg/Nm 3 ) 1 – 20 H 2 S (ppm) 5 – 50 Product Syngas Composition 3D CAD and Actual Photo of Gas Production Plant Control Panel for Gas Production Plant

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AbstractA large share of the agricultural biomass resource remains underutilized while local and national policies continueto mandate increasing levels of renewable energy. Only a small fraction of the available agricultural residues arecurrently utilized for energy, even where sustainability would support it. This virtually untapped resource for energyhas struggled because it is low in energy density, diffusely located, and costly to transport to large, centralizedenergy facilities. The use of smaller on-site gasification systems to produce bio-syngas from agricultural biomassresidues shows promise for increasing resource utilization for displacement of fossil fuels. Bio-syngas generated inon-site systems can provide a direct energy substitution for natural gas in gas devices like boilers, dryers, heaters,engines, etc. Proliferation of these systems would help industrial and agricultural processing facilities trying todecrease their carbon emissions footprint, a large part of which comes from on-site natural gas usage. This projectshows the technical, economic, and environmental feasibilities associated with on-site conversion of residuebiomass to bio-syngas for fuel in industrial and agricultural applications. The project samples and characterizes thephysical, chemical, and thermal properties of the biomass residues and resulting bio-syngas from the CircleDraft®gasifier system being deployed for commercial operation by West Biofuels, LLC, and its development partner, INSEREnergia, S.P.A. The project develops the optimal feedstock and operational conditions required to deliver bio-syngasthat is compatible with common natural-gas devices used in industry. In addition, the market potential of the bio-char produced as a byproduct of the gasification process is reviewed. The optimized results are used to evaluate theoverall costs of using bio-syngas in comparison with current and forecast industrial natural-gas prices, to determinethe economic feasibility for commercial projects. The net environmental benefits including potential greenhouse gasemission reductions and carbon sequestration will be reviewed.

Project Goal: The goal of this project is to determine the feasibility of using currently underutilized agriculturalbiomass residues for conversion to synthetic gas to replace or blend with natural gas for direct, on-site industrialand agricultural use

References• Faussone, G.C. 2012. Biomass Gasification With CircleDraft Process. Published online in Wiley Online Library (wileyonlinelibrary.com). DOI 10.1002/ep.11608• Faussone, G.C. 2014. Personal Communication.• Tittmann, P., N. Parker, Q. Hart and B. Jenkins. 2008. Economic potential of California biomass resources for energy and biofuel. PIER Collaborative Report, California Energy Commission, Sacramento, CA.• U.S. Energy Information Administration (EIA). 2014. California Natural Gas Statistics. http://www.eia.gov/dnav/ng/hist/n3035ca2A.htm• USDA NASS. 2013. California Field Crop Review 34(2), 21 February, www.nass.usda.gov/ca.• Williams, R.B., et al. 2008. An Assessment of Biomass Resources in California, 2007. PIER Collaborative Report, California Energy Commission, Sacramento, CA.

ConclusionAn 2-MW thermal biomass gas production facility has been constructed and is being operated in California fordemonstration on both forest and agricultural biomass feedstock. The produced gas is intended to be used as areplacement for natural gas in typical gas appliances used by the processing industries. While the project is ongoing,early results indicate that the performance targets listed above are within the capabilities of the technology.

Acknowledgement: Funds for this project were provided by West Biofuels and the California Energy Commission under Grant Agreement Number: #14-01-11G

ON-SITE BIOMASS GASIFICATION AS A NATURAL GAS SUBSTITUTE

Dr. Matthew Summers, Dr. Chang-hsien Liao, Mr. Matthew Hart, West Biofuels LLC, Woodland, CA 95776 USADr. Gian Claudio Faussone, INSER Energia S.p.A., C.so Appio Claudio, 229/5, Torino 10146 ITALY

Dr. Reinhard Seiser, Dr. Robert Cattolica, University of California at San Diego, La Jolla, CA 92093 USA

Project Tasks Performance / Cost Objectives1) Experimental design and selection and characterization of available biomass residues from agricultural sector

At least 3 specific biomass residues will be selected for potential suitability for gasification via the CircleDraft® gasifier system that meet criteria for high-quality gasification. The experimental design will be developed to determine the performance and the gas quality from each feedstock at various operating conditions.

Performance targets: Statewide Availability: 1 million tons/year aggregate; Cost: < $30 per ton; Moisture Content: < 25%; Ash Content: < 5%; Higher Heating Value: > 7,000 BTU/lb; Ash Melting Temperature: >1100°C; Particle Size: < 3 in.

2) Setup measurement systems to characterize performance and gas quality on a commercial CircleDraft® gasifier system

A CircleDraft® gasifier system will be provided by West Biofuels that nominally produces 6.75 MMBTU/hr of synthetic gas from 1000 pounds per hour of dry wood chips and will be outfitted with sensors and sampling ports so that the performance and gas quality can be analyzed for the selected residue feedstock.

Performance targets: Feedstock: mass flow measurement to ± 5% and composition to ± 3%; Gas: flow measurement to ± 10% and characterize 99% of major and trace gases; Energy: heating value to ±3% for feedstock and synthetic gas.

3) Conduct testing of biomass feedstock for performance and gas quality with CircleDraft® gasifier system

Tests with each feedstock will be conducted with the CircleDraft®

gasifier system over a range of selected operating conditions from the experimental design and the performance of the gasifier will be measured and the gas quality characterized.

Performance targets: Gasifier efficiency: >70%; Gas heating value: 150-300 BTU/SCF; Gas inert content: <60%; Gas impurities: Less than air quality and manufacturer requirements;

4) Analysis of technical and economic feasibility of natural gas replacement

Based on the optimal results from Task 3, the technical and economic feasibility of industrial or agricultural on-site gasifier projects for the replacement of natural gas will be developed.

Performance targets: Compatibility with natural gas devices (boilers/engines); Gasifier system capital cost: <$100,000 per MMBTU/hr capacity; Operating hours: 7000/year; Synthetic gas cost: $6-$12/MMBTU; Project simple payback: 3-6 years;

Agricultural Biomass Potential

TypeCurrent Industry

Energy Usage

BCHP Energy Production Potential*

Net Energy Potential

Power (GWh)

744 1366 622

Power Value($)

-$120 M @ $0.16/kWh

$188 M$68M @

$0.11/kWhNatural Gas

(BCF)14.9 49 34.1

Nat Gas Value ($)

-$119 M @ $8/1000 ft3 $255 M

$136 M @ $4/1000 ft3

* From Estimated 825,000 BDT of almond shell and 750,000 BDT of prunings.

California Biomass Feedstock Potential

California Almond Industry Energy Potential vs. Current Usage

Almond Shell Almond Pruning

The CircleDraft® Gasification Process

CircleDraft® Gasifier

Process Unit Specifications

Description Value

Fuel Type Chips, Shells, Residue Pellets & Cubes

Oxidant Humidified Air

Fuel Heating Value 8,500 BTU/dry lb

Moisture 25%

Specific Consumption 150 lbs/MMBTU

Gas Production Rate 45 SCF/dry lb

Gas Heating Value 150 BTU/SCF

Fuel Consumption ~ 1000 lbs/hr

Total Gas Output 6.75 MMBTU/hr

Electrical Consumption 90 kW

Working Temperatures 350 °C -1050 °C

Pressure Max: 20 in H2O

Thermal Efficiency 75%

Erection of Gasifier Structure Fabrication of Lower Grate Housing

Upper Reactor with Feeder Lower Cone Hot Face Refractory

Lower Cone Prior to Grate Installation Modular Control Room Fabrication

Plant Construction

Synthetic Gas Characteristic

CircleDraft® Range

H2 10 - 35%

CO 15 - 48%

CH4 1 - 4%

C2H4 0.1 - 0.5%

C3+ 0.1 - 0.3%

CO2 0.1 – 15%

N2 15 - 49%

H2/CO Ratio 0.5 – 1.5

HHV (MJ/Nm3) [BTU/scf] 5.6 – 10.3 [150 - 300]

Wobbe Index (MJ/Nm3) 22 – 38

Tars (mg/Nm3) 5 - 25

Particulate (mg/Nm3) 1 – 20

H2S (ppm) 5 – 50

Product Syngas Composition

3D CAD and Actual Photo of Gas Production PlantControl Panel for Gas Production Plant