SBIR/STTR Research Award

Membrane Process for solvent Reclamation and Reuse

Award identifier dc791138d62e4be5c52681a9d7bf2ee511af2c7a21e5a58159d6cc956a3ee72bAwarding agency Environmental Protection Agency

Award amount

$80,000

Program and phase

SBIR · Phase I

Award year

2012

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Award details

Awarding agency
Environmental Protection Agency
Branch
Not reported
Recipient company
MEMBRANE TECHNOLOGY AND RESEARCH, INC.
Proposal award date
2012-03-01
Contract end date
2012-08-31
UEI
JZ1RVB5TNLX9
Solicitation number
Not reported
Topic code
C

Research abstract

Many commercial hydrophilic solvents form azeotropes or have vapor-liquid equilibrium (VLE) pinch points with water, which making solvent recovery by conventional distillation difficult. Solvents that form such azeotropes or have such pinch points include isopropyl alcohol (IPA), acetone, methyl ethyl ketone (MEK), ethyl acetate, ethanol, butanol and tetrahydrofuran. Molecular sieve drying is possible, but requires intensive energy consumption for vaporization of the solvent/water mixture, and is generally not economical for situations where water concentration is more than 5 wt%. The process to be developed in this project uses pervaporative dehydration to reclaim and reuse solvents on-site. Membranes newly developed at MTR will be used. Compared to conventional membranes, the new membranes have superior thermal and chemical stability, and can deliver better solvent/water separations. The membrane modules will be adapted for counter-flow sweep operation to further extend the range of water concentrations that can be separated economically. In the Phase I project, the feasibility of the process will be determined, using IPA as a model solvent. IPA was chosen because it is widely used as a drying agent in the chemical, semiconductor, and electronics industries, and in the production of precision metal parts. Currently, the spent IPA is disposed of as hazardous waste, at a cost of about $20/gal. Virgin, high-purity IPA costs $10/gal, so the total cost of IPA used as a cleaning/drying agent is in the range of $30/gal. A considerable economic and environmental driving force exists to recover and reuse the IPA solvent. By the end of Phase I, at least one potential customer interested in participating in a Phase II IPA field test will be identified. Following successful field trials in Phase II, a commercialization plan will be developed to bring the new membrane technology to market. IPA recovery is our introductory target application, but once developed and demonstrated, the technology will be applicable to a wide variety of similar solvent recovery applications.

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.

Research funding history

191 SBIR/STTR records share this UEI (1983–2016). Reported award amounts total $31,990,487. Reported amounts are not federal obligations.

Phases: Phase I, Phase II

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

Agency intelligence

Environmental Protection Agency

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