合成气在K－F－MnO／Silicalite－2催化剂上转化为低碳烯烃的研究──Ⅳ．模试放大试验效应  

Investigation on Conversion of syngas to light alkenes over K-Fe-MnO/Sillcalite-2 catalyst Ⅳ. Effect of scaling-up on behavior of the catalyst

作　　者：徐龙伢[1] 王清遐[1] 杨力[1] 王开立[1] 赵修松[1] 

机构地区：[1]中国科学院大连化学物理研究所

出　　处：《天然气化工—C1化学与化工》1995年第4期21-25,共5页Natural Gas Chemical Industry

基　　金：国家"八.五"重点科技攻关课题

摘　　要：Ｋ－Ｆｅ－ＭｎＯ／Ｓｉｌｉｃａｌｉｔｅ－２催化剂经１００ｍｌ模试反应装置评价表明，其ＣＯ加氢制低碳烯烃反应性能可达到小试结果，且反应温度可降低５０～６０℃，催化剂具有良好的操作稳定性；提高反应温度（尤其是反应器入口温度）将导致低碳烯烃选择性大幅度下降，增加反应气空速有利于提高低碳烯烃选择性，而增大反应压力则不利于提高其选择性。erformance evaluation of K-Fe-MnO/silicalite-2 catalyst in the 100ml scaling-up reactor shows that the reactivity in productionof light olgfins via CO hydrogenation can bethe same as in the 6ml small reactor,the reaction temperature can be reduced by 50￣60℃,and the catalyst exhibits excellent stablecatalytic behavior. It will cause the olefin selectivity to decrease greatly to increase the reaction temperature (the reactor inlet temperature, in especial ), It is favourable to the increase of the light olefin selectivity to raise thegas space velocity,whereas it is unfavourableto it to enhance the reaction pressure.

关 键 词：合成气 烯烃 模试放大 分子筛 铁 氧化锰 

分 类 号：TE665.3[石油与天然气工程—油气加工工程]