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

助剂Fe和反应修饰剂修饰的Ru催化剂上苯选择加氢制环己烯
引用本文:孙海杰,李帅辉,田翔宇,张元馨,江厚兵,刘仲毅.助剂Fe和反应修饰剂修饰的Ru催化剂上苯选择加氢制环己烯[J].分子催化,2013,27(4):362-370.
作者姓名:孙海杰  李帅辉  田翔宇  张元馨  江厚兵  刘仲毅
作者单位:1. 郑州大学化学与分子工程学院,河南郑州450001;郑州师范学院化学系环境与催化工程研究所,河南郑州450044
2. 郑州大学化学与分子工程学院,河南郑州,450001
3. 郑州大学基础医学院,河南郑州,450001
基金项目:国家自然科学基金项目(面上项目,重点项目,重大项目);中国博士后科学基金
摘    要:共沉淀法制备了Ru-Fe(x)催化剂,并利用X射线衍射(XRD)、X射线荧光光谱(XRF)、N2物理吸附和透射电镜等手段对催化剂进行了表征.结果表明,Ru-Fe(x)催化剂中助剂Fe以Fe3O4形式存在.单独Fe3O4并不能提高Ru催化剂的环己烯选择性.但在加氢过程中Fe3O4可与反应修饰剂ZnSO4反应生成(Zn(OH)2)3(ZnSO4)(H2O)x(x=1 or 3).化学吸附的(Zn(OH)2)3(ZnSO4)(H2O)x(x=1 or 3)在提高Ru催化剂环己烯选择性中起着关键作用.此外,Ru-Fe(x)催化剂的性能还与浆液中的Zn2+浓度和pH值有关.在0.61 mol/L ZnSO4溶液中Ru-Fe(0.47)催化剂不但给出了56.7%的环己烯收率,而且具有良好的稳定性和重复使用性能.化学吸附在Ru表面的Fe2+同样能提高Ru催化剂的环己烯选择性.在0.29 mol/L和0.61 mol/L FeSO4溶液中Ru-Fe(0.47)催化剂上化学吸附Fe2+量近似,性能近似.因为Fe2+和Zn2+性质的差异,在0.29 mol/L和0.61 mol/L FeSO4溶液中Ru-Fe(0.47)催化剂的环己烯选择性分别低于在同浓度的ZnSO4溶液中的.

关 键 词:  选择加氢  环己烯  Ru-Fe催化剂
收稿时间:5/9/2013 12:00:00 AM
修稿时间:7/6/2013 12:00:00 AM

Selective hydrogenation of benzene to cyclohexene over the Ru catalyst modified by the promoter Fe and the reaction modifiers
SUN Hai-jie,LI Shuai-hui,TIAN Xiang-yu,ZHANG Yuan-xin,JIANG Hou-bing,LIU Shou-chang,LIU Zhong-yi.Selective hydrogenation of benzene to cyclohexene over the Ru catalyst modified by the promoter Fe and the reaction modifiers[J].Journal of Molecular Catalysis (China),2013,27(4):362-370.
Authors:SUN Hai-jie  LI Shuai-hui  TIAN Xiang-yu  ZHANG Yuan-xin  JIANG Hou-bing  LIU Shou-chang  LIU Zhong-yi
Institution:Zhengzhou University,Zhengzhou University,Zhengzhou University,Zhengzhou University,Zhengzhou University,Zhengzhou University
Abstract:The Ru-Fe(x) catalysts were prepared by a co-precipitation method. The catalysts were characterized by X-ray diffraction (XRD), X-fluorescence (XRF), N2 physisorption and transimission electron microscopy (TEM). The results showed that the promoter Fe existed as Fe3O4 in the catalysts. The Fe3O4 alone could not improve the selectivity to cyclohexene of Ru catalyst. However, the Fe3O4 on the surface could react with the reaction modifier ZnSO4 to form the (Zn(OH)2)3(ZnSO4)(H2O)x (x=1 or 3) salt. The chemisorbed (Zn(OH)2)3(ZnSO4)(H2O)x (x=1 or 3) salt played a key role in improving the selectivity to cyclohexene. Besides, the performance of the Ru-Fe(0.47) catalyst was closely related to the concentration of Zn2 and the pH values of the slurry. The Ru-Fe(0.47) catalyst gave a cyclohexene yield of 56.7% in the presence of 0.61 M ZnSO4. The reaction modifier FeSO4 also could enhance the selectivity to cyclohexene of the Ru-Fe(0.47) catalyst since the chemisorbed Fe2 could not be reduce to the metallic Fe on Ru surface. The Ru-Fe(0.47) catalyst exhibited the similar performance in 0.29 M and 0.61 M of FeSO4 solutions due to the similar amounts of the chemisorbed Fe2 . The Ru-Fe(0.47) catalyst showed the lower selectivity to cyclohexene in 0.29 M and 0.61 M of ZnSO4 solutions than that in the same concentrations of ZnSO4 for the different natures of Fe2 and Zn2 .
Keywords:benzene  selective hydrogenation  cyclohexene  Ru-Fe catalyst
本文献已被 CNKI 万方数据 等数据库收录!
点击此处可从《分子催化》浏览原始摘要信息
点击此处可从《分子催化》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