Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst (Articolo in rivista)

Type

• Articolo in rivista (Classe)
• Prodotto della ricerca (Classe)

Label

• Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst (Articolo in rivista) (literal)

Anno

• 2008-01-01T00:00:00+01:00 (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#doi

• 10.1016/j.cattod.2008.03.015 (literal)

Alternative label

• Basile, A., Tosti, S., Parmaliana, A., Iulianelli, A., Gallucci, F., Espro, C., Sporen, J. (2008)
  Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst
  in Catalysis Today
  (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#autori

• Basile, A., Tosti, S., Parmaliana, A., Iulianelli, A., Gallucci, F., Espro, C., Sporen, J. (literal)

Pagina inizio

• 17 (literal)

Pagina fine

• 22 (literal)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#numeroVolume

• 137 (literal)

Rivista

• Catalysis Today (Rivista)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#note

• DOI: 10.1007/s11244-008-9128-6. (literal)

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 Department of Industrial Chemistry, University of Messina, via Sperone 29, 98166 Messina, Italy c ENEA, Unita` Tecnico Scientifica Fusione, C.R. ENEA Frascati, via E. Fermi 45, Frascati, 00044 Roma, Italy (literal)

Titolo

• Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst (literal)

Abstract

• The methanol steam reforming (MSR) reaction was studied by using both a dense Pd-Ag membrane reactor (MR) and a fixed bed reactor (FBR). Both the FBR and the MR were packed with a new catalyst based on CuOAl2O3ZnOMgO, having an upper temperature limit of around 350 8C. A constant sweep gas flow rate in counter-current mode was used in MR and the experiments were carried out by varying the water/methanol feed molar ratio in the range 3/1-9/1 and the reaction temperature in the range 250- 300 8C. The catalyst shows high activity and selectivity towards the CO2 and the H2 formation in the temperature range investigated. Under the same operative conditions, the MR shows higher conversions than FBR and, in particular, at 300 8C and H2O/CH3OH molar ratio higher than 5/1 the MR shows complete methanol conversion. (literal)

Prodotto di

• Produzione di idrogeno per celle a combustibile (PM.P02.007.005) (Modulo)
• Institute on membrane technology (ITM) (Istituto)

Autore CNR

• ANGELO BRUNO BASILE (Unità di personale interno)
• ADOLFO IULIANELLI (Persona)
• FAUSTO GALLUCCI (Persona)

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• Parole chiave di "Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst" (Insieme di parole chiave)

Incoming links:

Prodotto

• Institute on membrane technology (ITM) (Istituto)
• Produzione di idrogeno per celle a combustibile (PM.P02.007.005) (Modulo)

Autore CNR di

• ANGELO BRUNO BASILE (Unità di personale interno)
• FAUSTO GALLUCCI (Persona)
• ADOLFO IULIANELLI (Persona)

Http://www.cnr.it/ontology/cnr/pubblicazioni.owl#rivistaDi

• Catalysis Today (Rivista)

Insieme di parole chiave di

• Parole chiave di "Hydrogen production by methanol steam reforming carried out in membrane reactor on Cu/Zn/Mg-based catalyst" (Insieme di parole chiave)