SBIR/STTR Research Award

Novel Microporous Membranes for Hydrogen Separation from Hydrotreater Recycle Gas

Award identifier 11af5dee727ad339f0f846dea3e48c0a17bdfe035d63cb09d2a59decacabed35Awarding agency Department of Energy

Award amount

$100,000

Program and phase

SBIR · Phase I

Award year

2004

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Award details

Awarding agency
Department of Energy
Branch
Not reported
Recipient company
Trans Ionics Corporation
Proposal award date
Not reported
Contract end date
Not reported
UEI
Not reported
Solicitation number
DOE/SC-0075
Topic code
37

Research abstract

75137-The separation of hydrogen from refinery recycle streams is energy intensive in that it requires cooling and may require decompression of the streams prior to separation by either membranes or pressure swing adsorption. The recovered hydrogen must then be recompressed and reheated to process conditions. This project will develop a cost-effective, thin-film composite inorganic membrane to produce purified hydrogen at the temperature of the hydrotreater and with a small pressure driving force. As a consequence, a higher pressure permeate will be supplied, and a considerable amount of energy will be saved. Specific objectives include: (1) developing an ultra thin micro porous hydrogen separation membrane with a higher hydrogen permeation rate at a higher selectivity compared to existing materials, (2) demonstrating its utility in the separation of mixed hydrogen streams at elevated temperatures, and (3) scaling the membrane to commercially viable module sizes for testing in selected industrial sites. During Phase I several membrane materials will be synthesized, ground to submicron powders, and formed into a membrane with a thickness less than 20 microns. Then, a proprietary procedure will be used to apply this film to a micro porous support layer, fused to provide mechanical strength. The membranes will be characterized analytically; and their ability to separate hydrogen from nitrogen, at temperatures characteristic of refining operations (300 - 500¿ C), will be determined. Commercial Applications and Other Benefits as described by the awardee: It is estimated that U.S. refiners use more than 2 billion standard cubic feet per day of hydrogen in the removal of sulfur from gasoline and diesel fuel streams. Because hydrogen treat gas rates are higher than consumption rates, the reactor off-gas is left with substantial amounts of hydrogen, which must be purified before it is recycled. Thus, a major opportunity exists to commercialize the new membrane process in the refining industry (especially at a time when lower sulfur levels in transportation fuels are being mandated, requiring even more hydrogen to remove this sulfur.)

Technology keywords

Not reported

Agency intelligence

Department of Energy

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