SBIR/STTR Research Award

Novel Method for Conversion of Biomass to Fuel

Award identifier a6514f902e48a7aa779f691d35843214c4f74dea266ed1b6ca4218060be7629bAwarding agency Department of Energy

Award amount

$1,000,000

Program and phase

SBIR · Phase II

Award year

2014

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Award details

Awarding agency
Department of Energy
Branch
Not reported
Recipient company
TDA RESEARCH, INC.
Proposal award date
2014-08-15
Contract end date
2016-08-16
UEI
MK5ANJVWVZK7
Solicitation number
DE-FOA-0001019
Topic code
11b

Research abstract

Synthesis gas, a mixture of H2 and CO, is one of the top-ten platform chemicals produced from biomass and can be used to produce fuel-ethanol. However, existing heterogeneous catalysts have only a low selectivity for ethanol and produce too much low-value methane. As a result, the production of ethanol from syngas with heterogeneous catalysts is uneconomical. Our major breakthrough is the discovery of a homogeneous catalytic system that exhibits high selectivity for ethanol and produces one tenth the amount of methane as do heterogeneous catalysts. TDA Research has developed a homogeneous catalytic system that can produce ethanol from syngas at rates comparable to the best heterogeneous catalysts while producing less than 2-3% methane (heterogeneous catalysts produce 20-40% CH4). Our catalysts first convert syngas to methanol, which is homologized in-situ to ethanol. Acetic acid formed by CO-insertion into methanol reacts with methanol to form methyl acetate, which is subsequently hydrogenated to ethanol and methanol. The alcohols are separated downstream and the methanol is recycled. The only products exiting the reactor are ethanol, a small amount of 1-propanol, methanol (which is recycled) and a small amount of methane. At the same time, the water-gas shift reaction consumes water produced during alcohol synthesis to produce additional hydrogen. The goal of the Phase IIB project is to scale up our homogeneous syngas to ethanol process by a factor of 50 by designing and building a continuous flow reactor system. We have chosen a bubble column reactor to dissipate the large exothermic heat of reaction of ethanol synthesis. The bubble column will hold approximately 250 mL of homogeneous catalyst solution with another 250 mL in the circulation system. While obviously much smaller than an industrial reactor, this scale of reactor will sufficiently simulate a full scale bubble column so that we can make the kinetic and steady state measurements, and determine the heat and mass transfer characteristics of the system needed to perform a preliminary pilot plant design at the end of the Phase IIB project. Also, we will work with our industrial partners and perform a detailed techno-economic analysis of the process. Commercial Applications and Other Benefits: Corn based ethanol plants use a food to produce fuel. Thermochemical methods (such as our syngas-to-ethanol process) for making ethanol are attractive because they can use agricultural and other renewable (non-edible) waste streams to make ethanol.

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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