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用原位红外技术研究Ag-MoO3/ZrO2催化丙烯气相环氧化反应
引用本文:金国杰,郭杨龙,刘晓晖,姚伟,郭耘,卢冠忠.用原位红外技术研究Ag-MoO3/ZrO2催化丙烯气相环氧化反应[J].化学学报,2006,64(19):1941-1946.
作者姓名:金国杰  郭杨龙  刘晓晖  姚伟  郭耘  卢冠忠
作者单位:[1]结构可控先进功能材料及其制备教育部重点实验室华东理工大学工业催化研究所,上海200237 [2]中国石化上海石油化工研究院,上海201208
基金项目:国家自然科学基金;高等学校博士学科点专项科研项目;上海市重大及重点基础研究项目
摘    要:制备了对丙烯直接气相环氧化具有优良催化性能的Ag-MoO3/ZrO2催化剂, 采用原位FT-IR技术研究了丙烯、环氧丙烷及丙烯和氧气混合气在载体和催化剂上的吸附及反应行为. 研究表明, 丙烯在ZrO2载体和20%Ag-4%MoO3/ZrO2催化剂上吸附后, 均不发生化学反应, 而环氧丙烷在ZrO2载体上吸附后于400 ℃发生开环反应, 在20%Ag-4%MoO3/ZrO2催化剂上吸附后于300 ℃发生开环反应. 当丙烯和氧气混合气在ZrO2载体上共吸附后, 随着反应温度从室温升高至400 ℃, 二者开始反应生成CO2和H2O; 混合气在20%Ag-4%MoO3/ZrO2催化剂上共吸附后于350 ℃开始反应. 对比非负载型Ag-MoO3催化剂的研究结果可见, ZrO2载体的存在使催化剂的活性下降的同时, 提高了对产物环氧丙烷的选择性.

关 键 词:丙烯  气相环氧化  环氧丙烷  Ag-MoO3/ZrO2催化剂  原位红外光谱
收稿时间:03 13 2006 12:00AM
修稿时间:2006-03-132006-06-07

Study on the Direct Gas Phase Epoxidation of Propylene over Ag-MoO3/ZrO2 Catalyst by in situ FT-IR
JIN,Guo-Jie,GUO,Yang-Long,LIU,Xiao-Hui,YAO,Wei,GUO,Yun,LU,Guan-Zhong.Study on the Direct Gas Phase Epoxidation of Propylene over Ag-MoO3/ZrO2 Catalyst by in situ FT-IR[J].Acta Chimica Sinica,2006,64(19):1941-1946.
Authors:JIN  Guo-Jie  GUO  Yang-Long  LIU  Xiao-Hui  YAO  Wei  GUO  Yun  LU  Guan-Zhong
Institution:a Laboratory for Advanced Materials, Research Institute of lndustrial Catalysis, East China University of Science and Technology, Shanghai 200237;b Shanghai Research Institute of Petrochemical Technology, China Petroleum and Chemical Corporation, Shanghai 201208
Abstract:The Ag-MoO3/ZrO2 catalyst for the direct gas phase epoxidation of propylene was prepared. The in situ FT-IR technology was employed to study the adsorption and reaction behavior of propylene, propylene oxide (PO) and the mixture gas of propylene and oxygen on the surface of ZrO2 support and Ag-MoO3/ZrO2 catalyst. The studies show that propylene adsorbed on ZrO2 support or 20%Ag-4%MoO3/ZrO2 catalyst is stable. When the reaction temperature is more than 400 ℃, the ring-opening reaction of propylene oxide adsorbed on ZrO2 support happens; over the 20%Ag-4%MoO3/ZrO2 catalyst, the ring-opening reaction of adsorbed propylene oxide occurs at 300 ℃. As the reaction temperature rises to 400 ℃, propylene adsorbed reacts with oxygen adsorbed on ZrO2 support to form water and CO2; over the 20%Ag-4%MoO3/ZrO2 catalyst, this surface reaction just takes place at 350 ℃. Comparing with the unsupported Ag-MoO3 catalyst, the presence of ZrO2 support can increase the selectivity of PO and while decrease the conversion of propylene.
Keywords:propylene  gas phase epoxidation  propylene oxide  Ag-MoO3/ZrO2 catalyst  in situ FT-IR
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