CO Selox Reaction Using Y-type Zeolite Catalytic Membranes (Articolo in rivista)

Type
Label
  • CO Selox Reaction Using Y-type Zeolite Catalytic Membranes (Articolo in rivista) (literal)
Anno
  • 2006-01-01T00:00:00+01:00 (literal)
Alternative label
  • P. Bernardo; C. Algieri; G. Barbieri; and E. Drioli (2006)
    CO Selox Reaction Using Y-type Zeolite Catalytic Membranes
    in Korean Membrane Journal
    (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori
  • P. Bernardo; C. Algieri; G. Barbieri; and E. Drioli (literal)
Pagina inizio
  • 13 (literal)
Pagina fine
  • 20 (literal)
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  • http://itm.cnr.it (literal)
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  • 8 (literal)
Rivista
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#pagineTotali
  • 8 (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni
  • P. Bernardo: National Research Council of Italy-Institute for Membrane Technology (ITM CNR) Via Pietro BUCCI, The University of Calabria, cubo 17C, 87030 Rende CS, Italy C. Algieri: National Research Council of Italy-Institute for Membrane Technology (ITM CNR) Via Pietro BUCCI, The University of Calabria, cubo 17C, 87030 Rende CS, Italy G. Barbieri: National Research Council of Italy-Institute for Membrane Technology (ITM CNR) Via Pietro BUCCI, The University of Calabria, cubo 17C, 87030 Rende CS, Italy E. Drioli: National Research Council of Italy-Institute for Membrane Technology (ITM CNR) Via Pietro BUCCI, The University of Calabria, cubo 17C, 87030 Rende CS, Italy (literal)
Titolo
  • CO Selox Reaction Using Y-type Zeolite Catalytic Membranes (literal)
Abstract
  • The production of CO-free hydrogen streams for feeding PEM-Fuel Cells using catalytic zeolite membrane reactors was analysed by means of selective oxidation. Tubular FAU (Na-Y) zeolite membranes, prepared by a secondary growth method and Pt-loaded, were used in a flow-through MR configuration. The catalytic tests were carried out at 200oC and at different pressures with a simulated dry reformate shifted gas mixture (H2 ca. 60%, CO 1%, plus O2, N2, CO2). The operative O2/CO stoichiometric equivalent feed ratio was ? = 2. These catalytic tests, reducing the CO concentration down to 10~50 ppm, verified the possibility of MR integration after using a low temperature water-gas shift unit of a fuel processor to convert hydrocarbons into hydrogen-rich gas. (literal)
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