Preferential CO oxidation over a platinum ceria alumina catalyst in a microchannel reactor

We have demonstrated the application of a Pt/Al2O3/CeO2 catalyst into a microreactor to reduce the CO content by preferential oxidation in a H2 rich model gas mixture. At temperatures between 120 °C and 260 °C and CO:O2 ratios smaller than 0.7 CO conversion of up to 98% for CO2-selectivities of 20%–35% were reached. The maximum space time yield was about 0.35 mmol g−1 min−1. rease the CO conversion and CO2-selectivity the concept of adding air or an air + N2 mixture through microholes to the CO + H2 mixture has been investigated with the design of an SSMR (staged supply microreactor). It was found that the CO2 selectivity is higher compared to the case of feeding of all gases in one passage, but only for lower CO conversion rates. st results for the preferential oxidation reaction were obtained at low reactant partial pressures. We found that the highest CO conversion rates are reached at reactant partial pressures in the range between 1 and 5 mbar. These values can be locally reached for total flows with 1–2 vol.-% CO and O2 by feeding N2 into the coated microchannels and the reactant gases into the uncoated microchannels. In this case, CO and H2 are equally lowered and the CO oxidation may be favoured over the H2 oxidation steps. A strong argument supporting this assumption is our measurements with varying the H2 inlet stream.