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High-Temperature Water-Gas Shift Membrane Reactor Study.


DE2007916959

Publication Date 2007
Personal Author Ciocco, M. V.; Iyoha, O.; Enick, R. M.; Killmeyer, R. P.
Page Count 12
Abstract 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.
Keywords
  • Chemical reactors
  • Water gas processes
  • Shift processes
  • Membrane transport
  • Fossil fueled power plants
  • High temperature
  • Coal gasification
  • Hydrogen
  • Membranes
  • Palladium
  • Sulfides
  • Thermodynamic properties
  • Stability
Source Agency
  • Technical Information Center Oak Ridge Tennessee
Corporate Authors Department of Energy, Washington, DC. Office of Fossil Energy.; Department of Energy, Washington, DC.
Supplemental Notes Sponsored by Department of Energy, Washington, DC.
Document Type Technical Report
NTIS Issue Number 200805
High-Temperature Water-Gas Shift Membrane Reactor Study.
High-Temperature Water-Gas Shift Membrane Reactor Study.
DE2007916959

  • Chemical reactors
  • Water gas processes
  • Shift processes
  • Membrane transport
  • Fossil fueled power plants
  • High temperature
  • Coal gasification
  • Hydrogen
  • Membranes
  • Palladium
  • Sulfides
  • Thermodynamic properties
  • Stability
  • Technical Information Center Oak Ridge Tennessee
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