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dc.creatorGalvita, V. V.en
dc.creatorSemin, G. L.en
dc.creatorBelyaev, V. D.en
dc.creatorSemikolenov, V. A.en
dc.creatorTsiakaras, P.en
dc.creatorSobyanin, V. A.en
dc.date.accessioned2015-11-23T10:26:55Z
dc.date.available2015-11-23T10:26:55Z
dc.date.issued2001
dc.identifier10.1016/s0926-860x(01)00708-6
dc.identifier.issn0926-860X
dc.identifier.urihttp://hdl.handle.net/11615/27637
dc.description.abstractA two-layer fixed-bed catalytic reactor for syngas production by steam reforming of ethanol has been proposed. In the reactor, ethanol is first converted to a mixture of methane, carbon oxides and hydrogen over a Pd-based catalyst and then this mixture is converted to syngas over a Ni-based catalyst for methane steam reforming. It has been shown that the use of the two-layer fixed-bed reactor prevents coke formation and provides the syngas yield closed to equilibrium. (C) 2001 Elsevier Science B.V. All rights reserved.en
dc.source.uri<Go to ISI>://WOS:000171614000013
dc.subjectethanolen
dc.subjectsteam reformingen
dc.subjectsyngasen
dc.subjecttwo-layer fixed-bed reactoren
dc.subjectTHERMODYNAMIC ANALYSISen
dc.subjectHYDROGEN-PRODUCTIONen
dc.subjectCATALYSTSen
dc.subjectALCOHOLSen
dc.subjectCOPPERen
dc.subjectChemistry, Physicalen
dc.subjectEnvironmental Sciencesen
dc.titleSynthesis gas production by steam reforming of ethanolen
dc.typejournalArticleen


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