SBIR/STTR Research Award

STTR Phase I: Novel Chemically Resistant Membranes

Award identifier 18ab753c1c0087c01ee7dde81da9efd70e7ed1e888cfbf1f41dac21d51f50756Awarding agency National Science Foundation

Award amount

$150,000

Program and phase

STTR · Phase I

Award year

2008

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Award details

Awarding agency
National Science Foundation
Branch
Not reported
Recipient company
COMPACT MEMBRANE SYSTEMS, INC.
Proposal award date
Not reported
Contract end date
Not reported
UEI
JDNRH32DML47
Solicitation number
NSF 07-551
Topic code
AM

Research abstract

This Small Business Technology Transfer Phase I project will develop novel chemically and thermally stable, highly fluorinated mixed matrix polymeric membranes with high selectivity. The program's objective is to apply enhanced membrane separation as an alternative to distillation separations that deal with high temperature and aggressive chemicals. Distillation is a major separation process in the chemical industry and consumes significant energy and capital costs. Many aggressive chemicals are difficult to separate by distillation. While membranes offer potential, most are limited by difficulties with aggressive chemicals and temperature limitations. Compact Membrane Systems has developed a family of perfluorinated membranes featuring high temperature capability, ability to operate in aggressive chemicals, and high flux. The chemical process industry would benefit from perfluorinated membranes with high upper use temperatures of 240ýýC with improved separation factors. This program addresses this particular need by developing mixed matrix membrane having perfluorinated base polymer and highly fluorinated additives. By introducing greater quantities of additives as well as appropriate choice of additives, we expect to significantly modify flux and separation properties of the base perfluoropolymers while retaining their unique stability. The broader impact/commercial potential from this technology could reduce energy consumption in the chemical process industries. Distillation consumes one-third of chemical process industry energy. Enhanced membrane processes with superior chemical and thermal properties can be used to replace/improve many of these distillation separations. The largest market is the ethanol dewatering market. Ethanol is expected to grow to upwards of 40% of U.S. fuel. If this occurs the market is 50-60 billion gallons of fuel per year. This project could lead to an energy-efficient process to produce ethanol as well as reduce the energy consumption of the chemical process industries.

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

218 SBIR/STTR records share this UEI (1993–2021). Reported award amounts total $55,705,610. Reported amounts are not federal obligations.

Phases: Phase I, Phase II

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

Agency intelligence

National Science Foundation

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