FENG Xu, LIN Yu, ZHANG Cai-shun, HAN Jiao, QING Shao-jun, ZHANG Lei, GAO Zhi-xian, GUAN Guo-qing. Effects of hydrothermal reaction temperatures on the performance of CuO/CeO2 catalyst for hydrogen production from steam reforming methanol[J]. Journal of Fuel Chemistry and Technology, 2022, 50(7): 832-840. DOI: 10.19906/j.cnki.JFCT.2021096
Citation: FENG Xu, LIN Yu, ZHANG Cai-shun, HAN Jiao, QING Shao-jun, ZHANG Lei, GAO Zhi-xian, GUAN Guo-qing. Effects of hydrothermal reaction temperatures on the performance of CuO/CeO2 catalyst for hydrogen production from steam reforming methanol[J]. Journal of Fuel Chemistry and Technology, 2022, 50(7): 832-840. DOI: 10.19906/j.cnki.JFCT.2021096

Effects of hydrothermal reaction temperatures on the performance of CuO/CeO2 catalyst for hydrogen production from steam reforming methanol

  • Using cerium nitrate as the source material and urea as the precipitant, nanometer CeO2 carrier was prepared by hydrothermal method, and the microstructure of CeO2 carrier was controlled by changing the hydrothermal reaction temperature. Then the CuO/CeO2 catalytic material was prepared by loading CuO on the CeO2 carrier and evaluated in methanol steam reforming for hydrogen production. Based on the characterization data of low temperature nitrogen adsorption, XRD, H2-TPR and XPS, the effects of hydrothermal reaction temperature on the microstructure of CeO2, the structure of CuO/CeO2 catalytic material and the performance of methanol steam reforming were investigated. The results show that the nanometer CeO2 support prepared at 180 ℃ has a cubic fluorite structure. After loading CuO onto the CeO2, the obtained CuO/CeO2 catalyst exhibits better catalytic activity due to its stronger Cu-Ce interaction, lower reduction temperature of Cu species in the surface, and more oxygen vacancies on the surface of the catalyst. When the reaction temperature is 280 ℃, the molar ratio of water to alcohol (W/M) is 1.2, and the space velocity of methanol vapor gas (GHSV) is 800 h− 1, the methanol conversion rate can reach 91.0%, the mole fraction of CO in reforming gas is 1.29%.
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