dc.creator | Galvita, V. V. | en |
dc.creator | Semin, G. L. | en |
dc.creator | Belyaev, V. D. | en |
dc.creator | Semikolenov, V. A. | en |
dc.creator | Tsiakaras, P. | en |
dc.creator | Sobyanin, V. A. | en |
dc.date.accessioned | 2015-11-23T10:26:55Z | |
dc.date.available | 2015-11-23T10:26:55Z | |
dc.date.issued | 2001 | |
dc.identifier | 10.1016/s0926-860x(01)00708-6 | |
dc.identifier.issn | 0926-860X | |
dc.identifier.uri | http://hdl.handle.net/11615/27637 | |
dc.description.abstract | A 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.subject | ethanol | en |
dc.subject | steam reforming | en |
dc.subject | syngas | en |
dc.subject | two-layer fixed-bed reactor | en |
dc.subject | THERMODYNAMIC ANALYSIS | en |
dc.subject | HYDROGEN-PRODUCTION | en |
dc.subject | CATALYSTS | en |
dc.subject | ALCOHOLS | en |
dc.subject | COPPER | en |
dc.subject | Chemistry, Physical | en |
dc.subject | Environmental Sciences | en |
dc.title | Synthesis gas production by steam reforming of ethanol | en |
dc.type | journalArticle | en |