@prefix prodottidellaricerca: . @prefix istituto: . @prefix prodotto: . istituto:CDS099 prodottidellaricerca:prodotto prodotto:ID328654 . @prefix pubblicazioni: . @prefix ns4: . ns4:ID348078 pubblicazioni:rivistaDi prodotto:ID328654 . @prefix rdf: . @prefix retescientifica: . prodotto:ID328654 rdf:type retescientifica:ProdottoDellaRicerca , prodotto:TIPO1101 . @prefix rdfs: . prodotto:ID328654 rdfs:label "Intensification of hydrogen production via methane reforming and the optimization of H2:CO ratio in a catalytic reactor with a hydrogen-permeable membrane wall (Articolo in rivista)"@en . @prefix xsd: . prodotto:ID328654 pubblicazioni:anno "1992-01-01T00:00:00+01:00"^^xsd:gYear ; pubblicazioni:doi "10.1016/0360-3199(92)90002-E"^^xsd:string . @prefix skos: . prodotto:ID328654 skos:altLabel "
Prokopiev S.I.; Aristov Yu.I.; Parmon V.N.; Giordano N. (1992)
Intensification of hydrogen production via methane reforming and the optimization of H2:CO ratio in a catalytic reactor with a hydrogen-permeable membrane wall
in International journal of hydrogen energy
"^^rdf:HTML ; pubblicazioni:autori "Prokopiev S.I.; Aristov Yu.I.; Parmon V.N.; Giordano N."^^xsd:string ; pubblicazioni:paginaInizio "275"^^xsd:string ; pubblicazioni:paginaFine "279"^^xsd:string ; pubblicazioni:url "http://www.scopus.com/inward/record.url?eid=2-s2.0-0026850107&partnerID=q2rCbXpz"^^xsd:string ; pubblicazioni:numeroVolume "17"^^xsd:string ; pubblicazioni:rivista ns4:ID348078 ; pubblicazioni:numeroFascicolo "4"^^xsd:string ; skos:note "Scopu"^^xsd:string ; pubblicazioni:affiliazioni "Institute of Catalysis, Akademika Lavrentieva pr., 5 Novosibirsk, 630090 Russia; Institute for Transformation and Storage of Energy, 98013 Pistunina, Messina, Italy"^^xsd:string ; pubblicazioni:titolo "Intensification of hydrogen production via methane reforming and the optimization of H2:CO ratio in a catalytic reactor with a hydrogen-permeable membrane wall"^^xsd:string ; prodottidellaricerca:abstract "The paper provides the results of a mathematical simulation of steam reforming of methane in a tubular catalytic reactor with a hydrogen-permeable wall. The influence of temperature (800-1100 K), pressure (0.1-2.0 MPa), the thickness of a palladium membrane (0.02-1.0 mm) and some other factors on the extent of methane conversion, hydrogen production rate and hydrogen-to-carbon monoxide ratio in the syngas produced are considered. The calculations have shown that under some optimal conditions the use of catalytic reactors with hydrogen-permeable walls allows an increase in the depth of the methane conversion and an acceleration of the formation of hydrogen in this process, as well as the production of syngas with the required composition. \u00A9 1992."@en ; prodottidellaricerca:prodottoDi istituto:CDS099 .