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Snytnikov, P.V.; Popova, M.M.; Men, Y.; Rebrov, E.V.; Kolb, G.; Hessel, V.; Schouten, J.C.; Sobyanin, V.A.
Applied catalysis. A, General, 11/2008, Letnik: 350, Številka: 1Journal Article
The activity of a 5 wt% Cu/CeO 2− x catalyst during preferential CO oxidation in hydrogen-rich gas mixtures was studied in a microchannel reactor. An increase of the O 2 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 weight hour space velocity (WHSV) up to 275,000 cm 3 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. ▪ The activity of a 5-wt% Cu/CeO 2− 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 cm 3 g −1 h −1. Both the CO concentration and the temperature increased when the WHSV was increased from 50,000 to 500,000 cm 3 g −1 h −1. An increase of the O 2 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 cm 3 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.
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