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催化精馏法干气制乙苯新工艺的研究
引用本文:刘军霞,王云山,张吉瑞,刘耀芳.催化精馏法干气制乙苯新工艺的研究[J].石油化工,2003,32(4):269-272.
作者姓名:刘军霞  王云山  张吉瑞  刘耀芳
作者单位:1. 石油大学,北京,重质油加工国家重点实验室,北京,102249
2. 北京服装学院,化工研究所,北京,100029
摘    要:在改性的β沸石催化剂上研究了催化精馏法干气制乙苯的工艺过程,考察了各工艺参数对烷基化反应的影响,并提出了适宜的工艺条件:乙烯质量空速小于0 25h-1、进料苯烯摩尔比大于4、反应压力大于1 5MPa、反应温度150~180℃。在此条件下,乙烯转化率大于96%,乙苯选择性大于94%,反应产物中基本上无二甲苯生成。

关 键 词:催化精馏  干气  乙苯  β沸石催化剂  烷基化
文章编号:1000-8144(2003)04-0269-04
修稿时间:2002年10月8日

Study on Preparation of Ethylbenzene with Ethylene in Dry Gas by Catalytic Rectification
LIU Jun-xia ,WANG Yun-shan ,ZHANG Ji-rui ,LIU Yao-fang.Study on Preparation of Ethylbenzene with Ethylene in Dry Gas by Catalytic Rectification[J].Petrochemical Technology,2003,32(4):269-272.
Authors:LIU Jun-xia  WANG Yun-shan  ZHANG Ji-rui  LIU Yao-fang
Affiliation:LIU Jun-xia 1,WANG Yun-shan 2,ZHANG Ji-rui 2,LIU Yao-fang 1
Abstract:Preparation of ethylbenzene with ethylene in dry gas by catalytic rectification process over zeolite β was studied. Effects of technological parameters on the alkylation were investigated. Preferred operating conditions were: ethylene WHSV ≤0 25 h -1 , feed mole ratio of benzene/ethylene≥4, pressure≥1 5 MPa and temperaure 150~180 ℃. Conversion of ethylene was over 96% and selectivity of ethylbenzene was over 94%. Moreover, dimethylbenzene was hardly found in the product.
Keywords:catalytic rectification  dry gas  ethylbenzene  β zeolite catalyst  alkylation
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