摘要
林原炼油厂于1996年底建成投产了一套30kt／a干气制乙苯装置。平稳运行3个多月，乙烯转化率大于90％，乙烯生成乙苯的选择性在70％左右，乙苯产品纯度达99.60％。
The 30000t/yr ethylbezene unit using dry gas as feedstock was conducted and put into operation at the end of 1996 in Linyuan Refinery. During the three month smooth operation of the unit, the conversion of ethylene was more than 90%, the selectivity of ethylene to ethylbenzene was about 70% and the purity of product ethylbenzene reached up to 90. 6 %.
出处
《炼油设计》
1998年第1期12-15,共4页
Petroleum Refinery Engineering
关键词
干气
烷基化反应
乙苯装置
炼油厂
fluid catalytic cracking, dry gas, alkylation, ethylbenzene manufacturing, ethylbenzene unit,commercial scale, start up
