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

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 CuOAl 2O 3ZnOMgO, having an upper temperature limit of around 350 °C. A constant sweep gas flow ra...

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Bibliographic Details
Published inCatalysis today Vol. 137; no. 1; pp. 17 - 22
Main Authors Basile, A., Parmaliana, A., Tosti, S., Iulianelli, A., Gallucci, F., Espro, C., Spooren, J.
Format Journal Article Conference Proceeding
LanguageEnglish
Published Amsterdam Elsevier B.V 30.08.2008
Elsevier Science
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Summary: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 CuOAl 2O 3ZnOMgO, having an upper temperature limit of around 350 °C. 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 °C. The catalyst shows high activity and selectivity towards the CO 2 and the H 2 formation in the temperature range investigated. Under the same operative conditions, the MR shows higher conversions than FBR and, in particular, at 300 °C and H 2O/CH 3OH molar ratio higher than 5/1 the MR shows complete methanol conversion.
ISSN:0920-5861
1873-4308
DOI:10.1016/j.cattod.2008.03.015