Hydrogen separation by dense cermet membranes

Novel cermet (i.e. ceramic–metal composite) membranes have been developed to separate hydrogen from mixed gases, particularly product streams generated during coal gasification and/or methane reforming. Hydrogen separation with these membranes is non-galvanic, i.e. it does not use electrodes or an e...

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Bibliographic Details
Published in:Fuel (Guildford) Vol. 85; no. 2; pp. 150 - 155
Main Authors: Balachandran, U., Lee, T.H., Chen, L., Song, S.J., Picciolo, J.J., Dorris, S.E.
Format: Journal Article Conference Proceeding
Language:English
Published: Oxford Elsevier Ltd 2006
Elsevier
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Summary:Novel cermet (i.e. ceramic–metal composite) membranes have been developed to separate hydrogen from mixed gases, particularly product streams generated during coal gasification and/or methane reforming. Hydrogen separation with these membranes is non-galvanic, i.e. it does not use electrodes or an external power supply to drive the separation, and hydrogen selectivity is nearly 100% because the membranes contain no interconnected porosity. The hydrogen permeation rate has been measured as a function of temperature (500–900 °C), membrane thickness (≈22–210 μm), and partial pressure of hydrogen (0.04–1.0 atm) in the feed gas. The hydrogen flux varied linearly with the inverse of membrane thickness, and reached ≈20 cm 3(STP)/min cm 2 for a membrane with a thickness of ≈22 μm at 900 °C with 100% H 2 (at ambient pressure) as the feed gas. The results indicate that the hydrogen flux is limited by bulk diffusion and might be higher for a thinner (<22 μm) membrane. Some of the membranes were tested in a simulated syngas mixture containing H 2, CO, CO 2, and CH 4, and showed no degradation in performance. Hydrogen flux measurements made in H 2S-containing atmospheres for times approaching ≈270 h showed that a 200-μm-thick cermet membrane was stable in gases containing up to ≈400 ppm H 2S. While longer-term studies are needed, these results suggest that the cermet membranes may be suitable for practical hydrogen separation applications.
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ISSN:0016-2361
1873-7153
DOI:10.1016/j.fuel.2005.05.027