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- W2001554734 abstract "The activity of a 5-wt% Cu/CeO2−x catalyst during preferential CO oxidation in hydrogen-rich gas mixtures was studied in a microchannel reactor. The CO concentration dropped from 1 vol.% to 10 ppm at a selectivity of 60%, at a temperature of 190 °C, and a weight hour space velocity (WHSV) of 55,000 cm3 g−1 h−1. Both the CO concentration and the temperature increased when the WHSV was increased from 50,000 to 500,000 cm3 g−1 h−1. An increase of the O2 concentration from a 1.2 to 3 fold excess reduced the CO concentration to 10 ppm in a broad temperature interval of 50 °C at WHSVs up to 275,000 cm3 g−1 h−1. The preferential CO oxidation could be carried out at higher flow rates and at higher selectivities in the microchannel reactor compared to a fixed-bed flow reactor." @default.
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- W2001554734 date "2008-11-15" @default.
- W2001554734 modified "2023-10-16" @default.
- W2001554734 title "Preferential CO oxidation over a copper–cerium oxide catalyst in a microchannel reactor" @default.
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- W2001554734 doi "https://doi.org/10.1016/j.apcata.2008.07.036" @default.
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