摘要
在全混釜批式反应器（ＣＳＴＲ）中研究了Ｙ型分子筛催化剂作用下苯与长直链烯烃的烷基化反应，探讨了投料比对烯烃转化率以及温度对产物选择性的影响。在所设计的新型液固循环反应－再生流化床反应系统中。
The alkylation reaction of benzene with linear dodecene was investigated in a continuous stirred tank reactor (CSTR) using zeolite as catalyst. The influence of ratio of reaction agents on the conversion of dodecene and reaction temperature on selectivity of products was studied. A new liquid-solid circulating fluidized bed reactor (LSCFBR) was designed. The industrial feasibility for industrial benzene with industrial dodecene used in this new reactor was investigated.
出处
《化学反应工程与工艺》
CAS
CSCD
北大核心
1997年第2期190-193,共4页
Chemical Reaction Engineering and Technology
基金
国家自然科学基金
石油化工总公司基础研究基金
关键词
长直链
烷苯基
分子筛催化剂
烷基化
烯烃
Linear alkylbezene, Liquid-solid circulating fluidized bed, Zeolite catalyst, Reaction-regeneration
