Low-temperature methanol synthesis in a circulating slurry bubble reactor

By Zhang K.   Song H.   Sun D.   Li S.   Yang X.   Zhao Y.   Huang Z.   Wu Y.  

Fuel, Vol. 82, Iss. 2, 2003-01 ,pp. : 233-239

Elsevier

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EFFECTS OF VARIOUS PROCESS PARAMETERS ON TEMPERATURE PROFILE OF ADIABATIC FIXED BED REACTOR FOR PRODUCTION OF DIMETHYL ETHER (DME) FROM METHANOL

By Eliassi Ali  

Chemical Engineering Communications, Vol. 194, Iss. 11, 2007-11 ,pp. : 1495-1502

Taylor & Francis Ltd

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A COMPARISON OF A NOVEL RECUPERATIVE CONFIGURATION AND CONVENTIONAL METHANOL SYNTHESIS REACTOR

By Khademi M. H.   Rahimpour M. R.   Jahanmiri A.  

Chemical Engineering Communications, Vol. 199, Iss. 7, 2012-07 ,pp. : 889-911

Taylor & Francis Ltd

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Low-pressure DME synthesis with Cu-based hybrid catalysts using temperature-gradient reactor

By Omata K.   Watanabe Y.   Umegaki T.   Ishiguro G.   Yamada M.  

Fuel, Vol. 81, Iss. 11, 2002-07 ,pp. : 1605-1609

Elsevier

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Methanol steam reforming in supported Pd membrane reactor The supported Pd membrane is promising for the production of high-purity hydrogen from catalytic steam reforming of methanol. At the 35 o C reaction temperature, the catalyst activity and stability are promoted by increasing the alumina content. Here a compact doublejacketed reactor has generated high-purity hydrogen directly from steam reforming of methanol, with no need for external purification and a much higher recovery yield.

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Fuel Cells Bulletin, Vol. 4, Iss. 37, 2001-10 ,pp. : 12-12

Elsevier

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