首页 | 本学科首页   官方微博 | 高级检索  
     检索      

Effect of Dimethyl Ether Co-feed on Catalytic Performance of Methane Dehydroaromatization over Mo/HZSM-5 Catalyst
作者姓名:HuiyingChen  YonggangLi  WenjieShen  YideXu  XinheBao
作者单位:StateKeyLaboratoryofCatalysis,DalianInstituteofChemicalPhysics,ChineseAcademyofSciences,Dalian116023,China
基金项目:科技部资助项目,the Natural Science Foundation of China
摘    要:The effect of dimethyl ether (DME) co-feed on the catalytic performance of methane dehydroaxomatization (MDA) over 6Mo/HZSM-5 catalyst was investigated as a function of DME concentration under reaction conditions of T=1023 K, p=101 kPa and SV=1500 ml/(g.h). A high benzene yield wasobtained and the stability of the catalyst was improved by adding 1.5%DME to the CH4 feed. The C6H6 yield was as high as ca. 10% even after reaction for 6 h. The stability of the catalyst was further improved when DME concentration in the co-feed gas was increased to an appropriate value. TGA and TPO results of the used 6Mo/HZSM-5 catalyst showed that the amount of coke on the used catalyst was reduced and the chemical nature of the coke was changed. When 1.5%DME was added to the CH4 feed, the coke formed on the catalyst could be burned off more easily than that when only CH4 was used as reactant. It is supposed that the oxygen in DME may play a role in preventing the coke burnt off at lower temperature from transforming into the coke burnt off at higher temperature, which results in the improvement of the stability of the catalyst.

关 键 词:二甲醚  甲烷  脱氢芳构化作用  HZSM-5负载钼催化剂

Effect of Dimethyl Ether Co-feed on Catalytic Performance of Methane
HuiyingChen YonggangLi WenjieShen YideXu XinheBao.Effect of Dimethyl Ether Co-feed on Catalytic Performance of Methane[J].Journal of Natural Gas Chemistry,2004,13(3):160-166.
Authors:Huiying Chen  Yonggang Li  Wenjie Shen  Yide Xu  Xinhe Bao
Institution:State Key Laboratory of Catalysis, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, China
Abstract:The effect of dimethyl ether (DME) co-feed on the catalytic performance of methane dehy droaromatization (MDA) over 6Mo/HZSM-5 catalyst was investigated as a function of DME concentration under reaction conditions of T=1023 K, p=101 kPa and SV=1500 ml/(g·h). A high benzene yield was obtained and the stability of the catalyst was improved by adding 1.5%DME to the CH4 feed. The C6H6 yield was as high as ca. 10% even after reaction for 6 h. The stability of the catalyst was further improved when DME concentration in the co-feed gas was increased to an appropriate value.TGA and TPO results of the used 6Mo/HZSM-5 catalyst showed that the amount of coke on the used catalyst was reduced and the chemical nature of the coke was changed. When 1.5%DME was added to the CH4 feed, the coke formed on the catalyst could be burned off more easily than that when only CH4 was used as reactant.It is supposed that the oxygen in DME may play a role in preventing the coke burnt off at lower temperature from transforming into the coke burnt off at higher temperature, which results in the improvement of the stability of the catalyst.
Keywords:Mo/HZSM-5  methane dehydroaromatization (MDA)  dimethyl ether (DME)  co-feed
本文献已被 CNKI 维普 万方数据 等数据库收录!
点击此处可从《天然气化学杂志》浏览原始摘要信息
点击此处可从《天然气化学杂志》下载免费的PDF全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号