SBIR/STTR Research Award

Novel Method for Conversion of Biomass to Fuel

Award identifier 85d8dfc41af2c2ac745fbccae17fdd4f63550b2e5a2b60390d4cb5e2343169a0Awarding agency Department of Energy

Award amount

$1,000,000

Program and phase

SBIR · Phase II

Award year

2011

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Award details

Awarding agency
Department of Energy
Branch
Not reported
Recipient company
TDA RESEARCH, INC.
Proposal award date
2011-08-15
Contract end date
2013-08-14
UEI
MK5ANJVWVZK7
Solicitation number
DE-FOA-0000508
Topic code
11 b

Research abstract

The United States needs efficient and cost-effective methods to convert biomass into liquid transportation fuels. Thermochemical gasification of biomass into synthesis gas followed by catalytic conversion into liquid fuels is a promising approach. One particularly attractive liquid fuel is ethanol. However, the thermochemical conversion of biomass into ethanol has been sta lled by lack of a cata lyst that can eff iciently and selectively convert syngas into e thanol. Problems with conventional heterogeneous catalysts include very poor selectivity and the production of undesired sideproductsespecially methane. To overcome shortcomings of solid heterogeneous catalysts for direct conversion of synthesis gas into ethanol, in Phase I we developed a homogeneous catalyst dissolved in an ionic liquid that plays a part in stabilizing the catalyst, controlling selectivity, and providing temperature control. The Phase II project will optimize the homogeneous catalytic process for economic scale-up, enabling the use of biomass-derived synthesis gas for the large-scale production of fuel ethanol. Synthesis gas was converted into ethanol while minimizing production of undesired side productsespecially methane, by utilizing homogeneous catalysts of nonvolatile, inorganic metal anions dissolved and stabilized in a highly thermally conductive, nonvolatile, ionic liquid. The homogeneous system also catalyzed the water-gas shift reaction, chemically consuming water co-produced with the ethanol, allowing energy-efficient separation of the ethanol from the ionic liquid while simultaneously producing hydrogen and allowing use of syngas with a CO/hydrogen molecular ratio of 1/1 or less, compatible with compositions derived from biomass gasifiers. A preliminary techno-economic analysis was performed for a 110 million gallon/year ethanol plant, showing that the optimized process would be competitive with or superior to other means of ethanol production. The homogeneous catalytic process will be refined with modeling, catalyst optimization and testing. Process and economic analysis for scale-up will be done in collaboration with our Phase II partners, including a major ethanol producer that would adopt the technology if the experimental results and process analysis meet industry benchmarks. Commercial Applications or other Benefits: The existing market for fuel ethanol is enormous, with annual U.S. consumption of 13.1 billion gallons, and is expected to grow to 36 billion gallons by 2022.

Technology keywords

Not reported

Other awards by this recipient

Verified by the same UEI. These are other public SBIR/STTR award pages, not a merged company record.

Awards with the same topic code

Verified by an exact topic code match. This is not a text-similarity match.

Research funding history

951 SBIR/STTR records share this UEI (1988–2026). Reported award amounts total $317,960,224. Reported amounts are not federal obligations.

Phases: Phase I, Phase II, Phase II – Direct to Phase II

Agencies: Department of Defense, Department of Energy, National Aeronautics and Space Administration, Environmental Protection Agency, National Science Foundation, Department of Health and Human Services

Agency intelligence

Department of Energy

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