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外环流气升式反应器中催化丙烯环氧化反应
引用本文:苏雪丽,王保国,王春艳,吴玉龙,米镇涛.外环流气升式反应器中催化丙烯环氧化反应[J].化学工业与工程,2004,21(3):165-168.
作者姓名:苏雪丽  王保国  王春艳  吴玉龙  米镇涛
作者单位:天津大学化工学院,天津,300072;天津大学化工学院,天津,300072;天津大学化工学院,天津,300072;天津大学化工学院,天津,300072;天津大学化工学院,天津,300072
基金项目:国家重点基础科学研究计划(973)资助项目(G2000048005)
摘    要:本论文研究了外环流气升式反应器中TS-1催化丙烯环氧化反应,以单位催化剂空时收率为目标,进行了反应工艺条件的优化,考察了结构参数,上升管与下降管横截面积之比Ar Ad对反应的影响。

关 键 词:外环流气升式反应器  TS-1  丙烯环氧化反应  工艺条件  结构参数
文章编号:1004-9533(2004)03-0165-04
修稿时间:2003年3月12日

Propylene Epoxidation Catalyzed by TS-1 in External Airlift Reactors
SU Xue-li,WANG Bao-guo,WANG Chun-yan,WU Yu-long,MI Zhen-tao.Propylene Epoxidation Catalyzed by TS-1 in External Airlift Reactors[J].Chemical Industry and Engineering,2004,21(3):165-168.
Authors:SU Xue-li  WANG Bao-guo  WANG Chun-yan  WU Yu-long  MI Zhen-tao
Affiliation:(School of Chemical Engineering,Tianjin University,Tianjin 300072,China
Abstract:In this thesis,propylene epoxidation catalyzed by TS-1 in external airlift reactors was studied. Firstly,the operation parameters were investigated so as to achieve higher yield of propylene oxide per gram catalyst. The optimum results were as follows:The optimum catalyst content was 3%, the preferred liquid and gas flow rates were 2 times of 720mL.h~(-1) and 290mL.min~(-1) respectively.Secondly,the study of the influence of geometry parameter A _r/ A _d was carried out. Under the same ratio of reactor volume to liquid inlet flow rate, conversion, selectivity and yield of propylene oxide per gram catalyst decreased when A _r/ A _d increased. At the same liquid inlet flow rate, the result that conversion,selectivity reduce at a higher degree was obtained,which proved that mass transfer influenced the propylene epoxidation and the mass transfer was affected more by apparent gas velocity than by reaction time.
Keywords:external airlift reactor  TS-1  propylene epoxidation  operation parameter  geometry parameter
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