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作 者:魏树权[1] 张光林[1] 吴雪红[1] 彭德群[1] 曲风枫[1]
机构地区:[1]哈尔滨师范大学化学化工学院,黑龙江哈尔滨150025
出 处:《化学工程师》2012年第11期4-6,共3页Chemical Engineer
基 金:黑龙江省教育厅科学技术研究(面上)项目(11531244)
摘 要:本文采用高压固定床反应装置考察了添加2%稀土氧化物(La2O3和CeO2)的Cu-ZnO-Al2O3/HZSM-5催化剂CO2加氢一步合成二甲醚的催化性能。XRD和H2-TPR结果分析发现,添加稀土氧化物后阻止了部分Cu2+还原为非晶态Cu。在513K,反应压力为3.0MPa,反应空速为1000h-1的条件下,考察了CO2加氢一步合成二甲醚的催化性能。结果表明,添加La2O3和CeO2后,催化剂的催化活性以及二甲醚的选择性均大幅提高,反应20h,CO2转化率以及二甲醚选择性变化较小,说明该催化剂稳定性较好。Direct synthesis of dimethyl ether (DME) from carbon dioxide by catalytic hydrogenation on Cu- ZnO-A1203/HZSM-5 catalyst modified by rare earth oxides (La203 and CeO2) was studied with the high pressure fixed bed reactor. The XRD and H2-TPR results indicated that the reduction of little of Cu2 ion were prevented. The catalytic properties of the catalyst was investigated at the 513K temperature, 3MPa reaction pressure and 1000h-t space velocity. The higher CO2 conversion was obtained on the Cu-ZnO-A12OJHZSM-5 catalyst modified by rare earth oxides. The stability of amorphous catalyst Cu-ZnO-A1203-CeO2/HZSM-5 was investigated by follow reaction conditions: 513K, 3 MPa, feed gas mixture carbon dioxide: hydrogen=l:4, reaction space velocity: 1000hq. The results showed that the CO2 conversion and DME selectivity change to a lesser extent within 20 hours, indicat- ing better stability of the catalyst.
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