Co-current and counter-current modes for Methanol Steam Reforming Membrane Reactor: Experimental Study (Articolo in rivista)

Type
Label
  • Co-current and counter-current modes for Methanol Steam Reforming Membrane Reactor: Experimental Study (Articolo in rivista) (literal)
Anno
  • 2006-01-01T00:00:00+01:00 (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#doi
  • 10.1016/j.cattod.2006.05.086 (literal)
Alternative label
  • Basile, A., Tosti, S., Capannelli, G., Vitulli, G., Iulianelli, A., Gallucci, F., Drioli, E. (2006)
    Co-current and counter-current modes for Methanol Steam Reforming Membrane Reactor: Experimental Study
    in Catalysis Today
    (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori
  • Basile, A., Tosti, S., Capannelli, G., Vitulli, G., Iulianelli, A., Gallucci, F., Drioli, E. (literal)
Pagina inizio
  • 237 (literal)
Pagina fine
  • 245 (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#numeroVolume
  • 118 (literal)
Rivista
Note
  • ISI Web of Science (WOS) (literal)
Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#affiliazioni
  • a Institute on Membrane Technology, ITM-CNR, c/o University of Calabria, via P. Bucci, Cubo 17/C, 87030 Rende (CS), Italy b ENEA, Unita` Tecnico Scientifica Fusione, C.R. ENEA Frascati, via E. Fermi 45, Frascati, 00044 Roma, Italy c Dipartimento di Chimica e Chimica Industriale, University of Genova, via Dodecaneso 31, 16146 Genova, Italy d Istituto di Chimica dei Composti Organometallici, ICCOM-CNR, c/o University of Pisa, via Risorgimento 35, 50126 Pisa, Italy e Department of Chemical Engineering and Materials, University of Calabria, via P. Bucci Cubo 42/A, 87030 Rende (CS), Italy (literal)
Titolo
  • Co-current and counter-current modes for Methanol Steam Reforming Membrane Reactor: Experimental Study (literal)
Abstract
  • Abstract The methanol steam reforming (MSR) reaction to produce hydrogen was studied from an experimental point of view in membrane reactors (MRs). In order to investigate the behaviour of methanol conversion, the influence of the membrane characteristics, the sweep gas flow rate, as well as the influence of the operating temperature and the different flux configurations were analysed. Experimental results, in terms of methanol conversion as well as hydrogen production and gases selectivity in MRs and a traditional reactor (TR), are proposed. A set of values of key parameters to obtain the maximum hydrogen production is given. (literal)
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