摘要
使用工程软件Aspen Plus对以环己烷为夹带剂的反应共沸精馏合成丙酸丙酯的过程进行模拟,并优化了工艺流程。结果表明,当反应精馏塔的操作条件为精馏段6块板,反应段和提馏段都为7块板时,塔釜产品丙酸丙酯的摩尔质量分数高达99.41%。
Synthesis of n-propyl propionate(PROPRO) in reactive distillation with cyclohexane (CYH) as entrainer is simulated and optimized by Aspen Plus. The results show that the molar fraction of PROPRO in the bottom of reactive distillation is 99. 41% when the rectifying section has six stages, and the reaction section and stripping section both have seven stages.
出处
《现代化工》
CAS
CSCD
北大核心
2016年第2期156-158,共3页
Modern Chemical Industry
关键词
反应精馏
丙酸丙酯
环己烷
ASPEN
PLUS
reaction distillation
n-propyl propionate
reaction kinetics
cyclonexane
Aspen Plus