Effect of cerium incorporation into zirconia on the activity of Cu/ZrO2 for methanol synthesis via CO hydrogenation
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Effect of cerium incorporation into zirconia on the activity of Cu/ZrO2 for methanol synthesis via CO hydrogenation

Abstract

The effects of Ce incorporation into ZrO2 on the catalytic performance of Cu/ZrO2 for the hydrogenation of CO have been investigated. A Ce0.3Zr0.7O2 solid solution was synthesized by forced hydrolysis at low pH. After calcination at 873 K, XRD and Raman spectroscopy characterization indicated that the Ce0.3Zr0.7O2 had a t'' crystal structure. 1.2 wt percent Cu/Ce0.3Zr0.7O2 exhibited H2 consumption peaks at low temperature (< 473 K) during H2-TPR indicating a significant fraction (~; 70 percent) of Ce4+ is reduced to Ce3+. 1.2 wt percent Cu/Ce0.3Zr0.7O2 is 2.7 times more active for methanol synthesis than 1.2 wt percent Cu/m-ZrO2 at 3.0 MPa at temperatures between 473 and 523 K and exhibits a higher selectivity to methanol. In-situ infrared spectroscopy shows that, analogous to Cu/m-ZrO2, the primary surface species on Cu/Ce0.3Zr0.7O2 during CO hydrogenation are formate and methoxide species. A shift in the band position of the bridged methoxide species indicated that some of these groups were bonded to both Zr4+ and Ce3+ cations. For both catalysts, the rate-limiting step for methanol synthesis is the reductive elimination of methoxide species. The higher rate of methanol synthesis on Cu/Ce0.3Zr0.7O2 relative to Cu/m-ZrO2 was primarily due to a ~; 2.4 times higher apparent rate constant, kapp, for methoxide hydrogenation, which is attributed to the higher surface concentration of H atoms on the former catalyst. The increased capacity of the Ce-containing catalyst is attributed to interactions of H atoms with Ce-O pairs present at the surface of the oxide phase.

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