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作 者:江莉龙[1] 杨阳[1] 叶炳火[1] 魏可镁[1]
机构地区:[1]福州大学化肥催化剂国家工程研究中心,福建福州350002
出 处:《分子催化》2010年第2期147-152,共6页Journal of Molecular Catalysis(China)
基 金:福建省教育厅计划资助项目(JA09012);福建省发改委"小发明;小创造"资助项目
摘 要:以改性铝土矿为载体,采用等体积浸渍法,制备了Ni-Mn-Ce-k体系水煤气变换催化剂.通过TG、DTA、TPR和活性表征等方法,系统考察了制备和还原条件对催化剂水煤气变换性能的影响.结果表明:催化剂的优化制备工艺为:第一步浸渍组分Ni、Mn、Ce的盐溶液(其摩尔配比为8:7:4),焙烧温度500℃,第二步浸渍K的加入量为5%(W),还原最高温度为500℃,还原过程添加适量的水蒸气,制得的催化剂具有良好的催化性能和热稳定性能,优于国内外现行工业产品.The Multiple-metal Catalysts (Ni-Mn-Ce-K/bauxite) for Water-Gas Shift Reaction were prepared by equivalent-volumetric impregnation method, and characterized by TG, DTA and TPR. Meanwhile, systematic investigation was carried out to identify the optimum preparation and reduction parameters. The optimum process was as following: In the first impregnation step, the loading ratio of Ni : Mn: Ce was 8: 7 : 4 and the calcination temperature was 500 ℃ ; in the second impregnation step, the loading of K was 5 %, the reduction temperature was 500 ℃, besides a proper amount of steam was needed. As compared with the commercial catalysts, the Ni-MnCe-K/bauxite catalyst prepared and reduced under optimum conditions exhibits more excellent catalytic performance and thermal stability for water-gas-shift reaction.
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