林产化学与工业2017，Vol.37Issue(5)：88-92,5.DOI:10.3969/j.issn.0253-2417.2017.05.011
工业双戊烯连续精馏过程模拟
Simulation of Continuous Distillation of Industrial Dipentene
叶国梁1
作者信息
- 1. 福建青松股份有限公司,福建南平354200
- 折叠
摘要
Abstract
Continuous rectification of industrial dipentene in vacuum was simulated by Aspen plus .Effects of feed stage,reflux ratio,distillate to feed ratio and operation pressure on limonene purity and reboiler energy consumption were investigated and the optimum conditions for distillation were obtained as follows:the theoretical plate number 65, feed stage at thirtieth, reflux ratio 4:1, distillate to feed ratio 0.7, top stage pressure 6 kPa, and the clumn pressure drop 12 kPa.Limonene with the purity of 71.5%and the distillate to feed ratio of 70%was obtained in production experiment , which is similar to the simulation results .关键词
双戊烯/柠檬烯/精馏/模拟Key words
dipentene/limonene/distillation/simulation分类
化学化工引用本文复制引用
叶国梁..工业双戊烯连续精馏过程模拟[J].林产化学与工业,2017,37(5):88-92,5.
