CIESC Journal

• 化工学报 • 上一篇    下一篇

悬浮床催化蒸馏新工艺合成异丙苯

温朗友,闵恩泽,庞桂赐,于文友   

  1. 石油化工科学研究院!北京100083,石油化工科学研究院!北京100083,石油化工科学研究院!北京100083,石油化工科学研究院!北京100083
  • 出版日期:2000-02-25 发布日期:2000-02-25

SYNTHESIS OF CUMENE BY SUSPENSION CATALYTIC DISTILLATION PROCESS

Wen Langyou,Min Enze,Pang Guici and Yu Wenyou (Research Institute of Petrochemical Processing,Beijing 100083)   

  • Online:2000-02-25 Published:2000-02-25

摘要: 以丙烯与苯烷基化合成异丙苯作为模型反应 ,对悬浮床催化蒸馏新工艺进行了初步探索 .结果表明 ,只要选择合适的催化剂 ,新工艺不仅能够稳定运转 ,而且可在常压、低温和低苯烯比的条件下取得高转化率、高选择性的较好反应结果 .

Abstract: A novel catalytic distillation process using a catalyst suspension is studied with the alkylation of benzene with propylene as a model reaction This new process is designated as “suspension catalytic distillation” (SCD) Exploratory experiments indicate that SCD can be operated steadily as long as a suitable catalyst is used For the synthesis of cumene in the SCD process, 100% conversion of propylene with more than 90% selectivity to cumene can be obtained under very mild conditions: atmospheic pressure, low temperature (80—100 ℃), low benzene/olefin mole ratio (1 75—3) The cumene product has extremely high purity with both n propylbenzene and C 8 aromatic less than 100ppm Compared with conventional Catalytic Distillation,SCD has many advantages,such as:① No need to manufacture catalytic packing;② No need to shut down the unit to replace the spent catalyst;③ Mass and heat transfer are better with fine catalyst particle than catalytic packings The SCD process is an advanced new catalytic distillation technology and is prospective and obviously worthwhile for further R & D efforts.

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