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机构地区:[1]滨州学院化学化工系,山东滨州256603 [2]长春工业大学化学工程学院,吉林长春130012
出 处:《工业催化》2008年第8期60-64,共5页Industrial Catalysis
基 金:吉林省科技发展项目(20030703)
摘 要:制备了一种新型、无毒Cu-Zn-Ca/γ-Al2O3配合物催化剂。采用固定床反应器,进行糠醛常压气相催化加氢反应,考察反应温度、催化剂组成、空速和氢醛比等因素的影响。结果表明,在508K、空速0.32h^-1、还原温度保持(493-513)K、活化6h和氢醛物质的量比为10:1条件下,糠醛转化率达到98.90%,2-甲基呋喃选择性达92.30%,2-甲基呋喃收率达91.28%。作为一种新型的无Cr催化剂,无毒,无污染,可代替Cu-Cr催化剂用于糠醛加氢过程,高活性和高选择性地制取2-甲基呋喃。A new harmless Cu-Zn-Ca/γ-Al2O3 complex catalyst was prepared. The catalytic vapor-phase hydrogenation of fuffural to 2-methylfuran was studied in a fixed bed reactor, and the influential factors, such as reaction temperature, composition of catalyst, LHSV, hydrogena-to-furfural mole ratio, grain size of the catalyst, on conversion, selectivity and yield were investigated. Selectivity of over 99%, and yield of 97% were obtained for 2-methylfuran under the following condition: 508 K, LHSV 0.32 h^-1 , reduction temperature 493-513 K, activation for 6 h, n(hydrogen): n(furfural) = 10: 1. The catalyst, with high activity and excellent selectivity, could be a substitute for Cu-Cr catalysts for production of 2-methylfuran.
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