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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Published in | Catalysis today Vol. 137; no. 1; pp. 17 - 22 |
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Main Authors | , , , , , , |
Format | Journal Article Conference Proceeding |
Language | English |
Published |
Amsterdam
Elsevier B.V
30.08.2008
Elsevier Science |
Subjects | |
Online Access | Get full text |
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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. |
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ISSN: | 0920-5861 1873-4308 |
DOI: | 10.1016/j.cattod.2008.03.015 |