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• W2000573234 abstract "The heat transfer effects on a methanol-steam reforming (MSR) process are numerically investigated using a circular reformer with a partially (referred to as the wall-coated reformer) or entirely filled catalyst layer (referred to as the packed-bed reformer). The catalyst layer is formed by packing CuO/ZnO/Al2O3 catalyst particles with a certain porosity and permeability. The fluid flow characteristics are strongly affected by the catalyst-layer thickness. As a consequence, the heat and mass transfer also depend on the catalyst-layer thickness. Under heat supplied by wall heat flux conditions, it is found that higher reforming temperature can be obtained for the wall-coated reformer compared with the packed-bed reformer. This results in the wall-coated reformer having a better methanol conversion efficiency compared with the packed-bed reformer. Based on our study, the minimum heat transfer coefficient, maximum methanol conversion and maximum carbon monoxide production are obtained when the catalyst-layer thickness is 90% of the reformer radius." @default.
• W2000573234 created "2016-06-24" @default.
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• W2000573234 date "2009-07-01" @default.
• W2000573234 modified "2023-09-24" @default.
• W2000573234 title "Heat transfer effects on the methanol-steam reforming with partially filled catalyst layers" @default.
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• W2000573234 doi "https://doi.org/10.1016/j.ijhydene.2009.04.049" @default.
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