石油炼制与化工 ›› 2014, Vol. 45 ›› Issue (11): 29-32.

• 催化剂 • 上一篇    下一篇

Pd/CoSAPO-11催化剂的制备及其正丁烯异构化催化性能研究

刘彦峰1,杨晓东1,胡胜2,于春梅1   

  1. 1. 中国石油大庆化工研究中心
      2. 中国石油石油化工研究院
  • 收稿日期:2014-05-15 修回日期:2014-05-27 出版日期:2014-11-12 发布日期:2014-10-28
  • 通讯作者: 刘彦峰 E-mail:lyf459@petrochina.com.cn
  • 基金资助:

    中国石油天然气股份有限公司炼油与化工基金项目

PREPARATION OF Pd/ CoSAPO-11 CATALYST AND ITS n-BUTYLENE ISOMERIZATION PERFORMANCE

  • Received:2014-05-15 Revised:2014-05-27 Online:2014-11-12 Published:2014-10-28

摘要: 采用水热合成方法将Si和过渡元素Co同时引入AlPO-11磷酸铝分子筛骨架,合成出CoSAPO-11双原子取代型磷酸铝分子筛,并采用等体浸渍法将PdCl2溶液浸渍到载体上,制得Pd/CoSAPO-11催化剂,考察了温度和空速对Pd/CoSAPO-11催化剂上正丁烯异构化反应的影响,并与传统工业载体γ-Al2O3负载Pd催化剂对比。结果表明,以Pd/CoSAPO-11为催化剂,在反应温度为400℃、反应压力为5.0 MPa、体积空速为2.0~4.0 h-1的条件下,异丁烯选择为89.2%~93.1%,异丁烯产率为31.7%~34.5%,表现出比Pd/γ-Al2O3催化剂更好的正丁烯异构化性能。

Abstract: Double atom Si and Co-substituted AlPO-11 zeolite, CoSAPO-11, was synthesized in situ by hydrothermal method and the Pd/ CoSAPO-11 catalyst was then prepared by incipient wetness method using PdCl2 solution. The isomerization performance of n-butylene on the prepared catalyst was investigated at different temperatures and space velocities. Compared with the traditional commercial Pd/γ-Al2O3, Pd/CoSAPO-11 catalyst exhibits better n-butylene isomerization performance. The results show that at the optimal conditions: 400℃, 5.0 MPa and velocity of 2-4 h-1. The selectivity to isobutylene of the Pd/ CoSAPO-11 catalyst is up to 82.9%-93.1 % with the yield of 31.7%-34.5 %.