活性炭负载[Rh(COD)Cl]_2催化剂的制备及其催化性能
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  • 英文篇名:Preparation and Catalytic Properties of [Rh(COD)Cl]_2 Catalysts Supported on Activated Carbon
  • 作者:王红琴 ; 王亚明 ; 蒋丽红
  • 英文作者:WANG Hong-qin;WANG Ya-ming;JIANG Li-hong;Faculty of Chemical Engineering,Kunming University of Science and Technology;Sino-platinum Metals Co.Ltd.;
  • 关键词:β-蒎烯 ; 加氢反应 ; 活性炭 ; 负载型[Rh(COD)Cl]_2催化剂 ; 蒎烷 ; 催化与分离提纯技术
  • 英文关键词:beta-pinene;;hydrogenation reaction;;activated carbon;;supported [Rh(COD)Cl]_2 catalyst;;pinane;;catalysis;;separation and purification technology
  • 中文刊名:JXHG
  • 英文刊名:Fine Chemicals
  • 机构:昆明理工大学化学工程学院;贵研铂业股份有限公司;
  • 出版日期:2018-02-15
  • 出版单位:精细化工
  • 年:2018
  • 期:v.35
  • 基金:国家自然科学基金(21266012)~~
  • 语种:中文;
  • 页:JXHG201802011
  • 页数:9
  • CN:02
  • ISSN:21-1203/TQ
  • 分类号:72-80
摘要
以氧化活性炭(OAC)为载体、自制[Rh(COD)Cl]_2为活性组分,制备了负载型催化剂[Rh(COD)Cl]_2/OAC(COD为1,5-环辛二烯),用XPS、N2吸-脱附、FTIR等对其结构进行了表征与分析,以β-蒎烯加氢反应为探针反应,考察了载体种类、氧化剂HNO3浓度、[Rh(COD)Cl]_2与OAC质量比对负载型催化剂[Rh(COD)Cl]_2/OAC性能的影响,在此基础上优化了β-蒎烯加氢工艺条件,并测定了催化剂([Rh(COD)Cl]_2/OAC)的重复使用性。结果表明,催化剂的最佳制备条件为:氧化活性炭为较佳载体,HNO3浓度为7.23mol/L,[Rh(COD)Cl]_2与OAC质量比为1∶8.3,此时β-蒎烯转化率均值为99.94%;顺式蒎烷选择性(以只生成蒎烷计,下同)均值为88.64%;顺式蒎烷收率均值为88.59%;β-蒎烯加氢工艺的最佳条件为:反应温度50℃,反应压力3.5 MPa,催化剂用量为β-蒎烯质量的3.5%,反应时间4.0 h,此条件下β-蒎烯转化率均值为99.88%;顺式蒎烷选择性均值为89.00%;顺式蒎烷收率均值为88.90%,[Rh(COD)Cl]_2/OAC催化剂在β-蒎烯加氢反应中表现出较佳的催化活性。催化剂重复使用4次后,β-蒎烯转化率仍可达89.64%,活性组分Rh的流失是造成催化剂失活的主要原因。
        Supported [Rh(COD)Cl]_2/OAC catalysts were prepared by using oxidized activated carbon as support and self made [Rh(COD)Cl]_2 as active component( COD = 1,5-cyclooctadiene). The resulting catalysts were characterized by means of XPS,N2 adsorption-desorption and FTIR.Hydrogenation reaction of beta-pinene was used as a probe reaction to investigate the effects of carrier type,oxidant nitric acid concentration and mass ratio of [Rh(COD)Cl]_2 to OAC on the catalytic properties. On this basis,the hydrogenation conditions of beta-pinene were optimized,and the reusability of [Rh(COD)Cl]_2/OAC was measured. The experimental results indicated that the optimum preparation conditions of catalyst were as follows: oxidized activated carbon was used as support,nitric acid concentration was 7. 23 mol/L,and the mass ratio of [Rh(COD)Cl]_2 to OAC was 1∶ 8. 3. Under these conditions,the catalyst showed excellent catalytic activities in the hydrogenation reaction of beta-pinene. The average conversion of beta-pinene was 99. 88%,and the average selectivity and yield of cis-pinane were 89. 00% and 88. 90%. Additively,the [Rh(COD)Cl]_2/OAC stillremained high activities with a conversion of 89. 64% after being used for four times. The cause of deactivation of [Rh(COD)Cl]_2/OAC was that active component Rh was easy to lose in the running process.
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