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NAMS 2002 Workshop - ICOM 2008

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Gas Separation I – 5<br />

Monday July 14, 11:45 AM-12:15 PM, Kaua’i<br />

Development of High Temperature CO2-Selective Porous Ceramic<br />

Membranes<br />

A. Ku (Speaker), GE Global Research, Niskayuna, NY, USA, kua@research.ge.com<br />

V. Ramaswamy, GE Global Research, Niskayuna, NY, USA<br />

J. Ruud, GE Global Research, Niskayuna, NY, USA<br />

P. Willson, GE Global Research, Niskayuna, NY, USA<br />

K. Narang, GE Global Research, Niskayuna, NY, USA<br />

Because of their mechanical durability and thermal and chemical stability,<br />

inorganic membranes have the potential to increase the efficiency of industrial<br />

processes by enabling efficient separation of process gas streams into their<br />

constituents. Numerous industrial processes, including hydrocarbon processing,<br />

steam methane reforming, water gas shift, and CO2 capture from power<br />

generation systems, would benefit from gas separation membranes that operate<br />

at elevated temperatures. Selectivity is a key requirement for membranes. In<br />

general, porous membranes are more selective for the smaller or lighter<br />

molecules in a gas mixture. However, the mechanism of selective surface<br />

transport, due to gas adsorption on the pore walls, can increase the flux of the<br />

heavier molecule resulting in a reverse selective membrane.<br />

Surface transport of adsorbed CO2 can lead to CO2-selectivity in porous<br />

membranes, but is believed to be a low temperature effect because of desorption<br />

of the gas upon heating. We will describe efforts to develop porous ceramic<br />

membranes with enhanced surface transport of CO2 at elevated temperatures.<br />

Based on a conceptual framework that allows screening for promising materials<br />

through chemisorption properties, we identified several promising candidate<br />

oxides and fabricated supported microporous membranes. We will report the gas<br />

permeation and separation properties of our oxide membranes against a<br />

microporous silica benchmark with substantial room temperature CO2/H2<br />

selectivity.<br />

Acknowledgement: This material is based partly upon work that was supported<br />

by the U.S. Department of Energy under award number DE-FC26-05NT42451.

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