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High-Temperature Water-Gas Shift Membrane Reactor Study [electronic resource].

Published
Washington, D.C. : United States. Dept. of Energy, 2007.
Oak Ridge, Tenn. : Distributed by the Office of Scientific and Technical Information, U.S. Dept. of Energy.
Additional Creators
National Energy Technology Laboratory (U.S.), United States. Department of Energy, and United States. Department of Energy. Office of Scientific and Technical Information
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Summary
NETL’s Office of Research and Development is exploring the integration of membrane reactors into coal gasification plants as a way of increasing efficiency and reducing costs. Water-Gas Shift Reaction experiments were conducted in membrane reactors at conditions similar to those encountered at the outlet of a coal gasifier. The changes in reactant conversion and product selectivity due to the removal of hydrogen via the membrane reactor were quantified. Research was conducted to determine the influence of residence time and H2S on CO conversion in both Pd and Pd80wt%Cu membrane reactors. Effects of the hydrogen sulfide-to-hydrogen ratio on palladium and a palladium-copper alloy at high-temperature were also investigated. These results were compared to thermodynamic calculations for the stability of palladium sulfides.
Report Numbers
E 1.99:doe/netl-ir-2007-215
doe/netl-ir-2007-215
Subject(s)
Note
Published through SciTech Connect.
06/01/2007.
"doe/netl-ir-2007-215"
32nd International Technical Conference on Coal Utilization & Fuel Systems, Clearwater, FL, June 10-15, 2007.
Killmeyer, R.P.; Enick, R.M.; Iyoha, O.; Ciocco, M.V.
Funding Information
None cited
View MARC record | catkey: 14152535