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负载杂多酸催化剂催化合成直链烷基苯的研究
引用本文:朱佐刚,张金昌,李成岳. 负载杂多酸催化剂催化合成直链烷基苯的研究[J]. 北京化工大学学报(自然科学版), 2003, 30(4): 17-20
作者姓名:朱佐刚  张金昌  李成岳
作者单位:北京化工大学可控化学反应科学与技术教育部重点实验室,北京,100029
基金项目:国家研究发展基金;G2000048006;
摘    要:在固定床反应器和一定的反应条件下,考察了改变苯烯摩尔比对负载杂多酸催化剂催化合成直链烷基苯的活性和选择性的影响。实验结果表明,随着苯烯比的增加,十二烯的转化率和2位-十二烷基苯的选择性均有所增加。在苯烯摩尔比4∶1、液体质量总空速10h-1、温度120℃和液固反应条件下,对催化剂的稳定性进行了实验考察,结果显示,连续反应70h后,负载杂多酸催化剂的活性明显下降。利用SEM、FT-IR和TG等对失活催化剂进行了基本表征,结果表明积炭可能是引起负载杂多酸催化剂失活的主要原因。

关 键 词:直链烷基苯  固体酸  催化剂  失活  直链烷基苯   固体酸   催化剂   失活
修稿时间:2002-11-05

Catalytic synthesis of linear alkylbenzene using supported heteropoly acid catalyst
ZHU Zuo-gang ZHANG Jin-chang LI Cheng-yue. Catalytic synthesis of linear alkylbenzene using supported heteropoly acid catalyst[J]. Journal of Beijing University of Chemical Technology, 2003, 30(4): 17-20
Authors:ZHU Zuo-gang ZHANG Jin-chang LI Cheng-yue
Affiliation:The Key Laboratory of Science and Technology of Controllable Chemical Reactions; Ministry of Education; Beijing University of Chemical Technology; Beijing; China
Abstract:The influences of molar ratios of benzene to dodecene on catalytically synthesizing linear alkylbenzene using supported heteropoly acid catalyst was investigated at a fixed bed reactor and certain reaction conditions. It is showed that the conversion ratio of dodecene and the selectivity of producing 2-alkylbenzene are slightly increased with increasing molar ratio of benzene to dodecene, respectively. The catalyst stability was also investigated at the following reaction conditions. The molar ratio of benzene to dodecene was 4:1, total liquid space velocity 10 h-1.and the reaction temperature 120℃.The results show that the catalyst activity is obviously decreased after it is undergone continuously 70h reaction at the fixed bed reactor. The deactivated catalyst was characterized by SFM.FT-IR and TG. The results show that the probably reason resulting in the catalyst losing its activity is the polymers, which was produced during the alkylation process, deposited on the catalyticsites.
Keywords:linear alkylbenzene  solid acid  catalyst  deactivated
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