SBIR/STTR Research Award

Membrane-Sorbent Hybrid System for Post Combustion Carbon Capture

Award identifier 17bec19cba5959b716063a661f0fc800b7eda68906e457a410c3d4679e81f052Awarding agency Department of Energy

Award amount

$999,999

Program and phase

SBIR · Phase II

Award year

2015

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Award details

Awarding agency
Department of Energy
Branch
Not reported
Recipient company
TDA RESEARCH, INC.
Proposal award date
2015-07-27
Contract end date
2017-07-26
UEI
MK5ANJVWVZK7
Solicitation number
DE-FOA-0001258
Topic code
12e

Research abstract

The electricity produced from fossil fuels is essential to the worlds prosperity and security. On the other hand, increasing atmospheric CO2 concentration caused by the fossil fuel combustion are causing concerns regarding global warming. Although there are several methods for separating CO2 from the flue gases at existing coal-fired power plants, all of them have significant drawbacks, including loss of efficiency and increased capital and operating costs that dramatically increase the cost of electricity. TDA Research, Inc. (TDA), in collaboration with Membrane Technology Research Corporation and the University of California, Irvine are developing a low cost, high capacity sorbent that will integrate into a membrane-sorbent hybrid post-combustion carbon capture system to remove CO2 from coal-fired power plant effluents. In Phase I, we optimized the sorbent to meet the needs of the application. Our preliminary analysis results indicate the sorbent system operated in a concentration swing mode will have a significantly lower cost than an equivalent membrane system, increasing the economic viability of the carbon capture process. Sorbent improvements also enabled lower oxygen transfer rates from the boiler air intake side to the flue gas side. The process simulation suggested a plant efficiency of 29.74% for the hybrid system which is well above that can be achieved by the state-of-the-art amine scrubbing technology and the CO2 capture cost is estimated to be less than $42.2 per tonne on 2007 $ basis. In our Phase II work, we will work on further enhancing the CO2 capacity of the sorbent, while further reducing their oxygen affinity. We will assess the impact of critical parameters at bench- scale and carry out adsorption/desorption cycles (a minimum of 10,000 cycle test). We will then assess the performance of an integrated 2 to 5 scfm unit in the field using actual coal-derived flue gas. We will carry out the process simulation work and evaluate the techno-economic viability of the new CO2 capture technology retrofit to the existing pulverized coal power plants using the methodology described in NETLs Carbon Capture and Sequestration Systems Analysis Guidelines. CO2 is a major greenhouse gas and the most dominant source for the anthropogenic CO2 emissions. It is a by-product of the combustion of fossil fuels, in particular burning coal for generating electricity. The proposed technology will provide a cost effective way to control CO2 emissions from the existing and new coal-fired power plants. There will be a large market when legislation limiting or taxing carbon emissions is put in place.

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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