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分批精馏过渡段放持液操作方式
引用本文:张雪梅,何杰,张卫江,张志刚,简春贵,杨志才.分批精馏过渡段放持液操作方式[J].中国化学工程学报,2006,14(3):337-342.
作者姓名:张雪梅  何杰  张卫江  张志刚  简春贵  杨志才
作者单位:天津大学;天津大学;天津大学;天津大学;天津大学
摘    要:The new mode of operation for slop cut withdrawal in batch distillation, i.e., draining Column liquid holdup at the end of slop cut period, was proposed. And the stopping criterion for the operation was investigated, Experiments were carded out with isopropanol-n-propanol binary system and isopropanol-n-propanol-n-butanol ternary system in a distillation column with a liquid collector installed between the reboiler and the column section, Experimental results in a Ф 45mm batch column show that the proposed policy can overcome the flywheel effect caused by column liquid holdup and thus cut down operation time and energy consumption 31%-61%.

关 键 词:分批精馏  过渡段  操作方式  废馏分
收稿时间:2005-04-19
修稿时间:2005-04-192006-02-06

The Operation of Draining Column Holdup for Slop Cut Withdrawal in Batch Distillation
ZHANGXuemei,HEJie,ZHANGWeijiang,ZHANGZhigang,JIANChungui,YANGZhicai.The Operation of Draining Column Holdup for Slop Cut Withdrawal in Batch Distillation[J].Chinese Journal of Chemical Engineering,2006,14(3):337-342.
Authors:ZHANGXuemei  HEJie  ZHANGWeijiang  ZHANGZhigang  JIANChungui  YANGZhicai
Affiliation:a School of Chemical Engineering and Technology, Tianjin University, Tianjin 300072, China; b Tianjin Univtech Co. Ltd., Tianjin 300072, China
Abstract:The new mode of operation for slop cut withdrawal in batch distillation, i.e., draining column liquid holdup at the end of slop cut period, was proposed. And the stopping criterion for the operation was investigated. Experiments were carried out with isopropanol-n-propanol binary system and isopropanol-n-propanol-n-butanol ternary system in a distillation column with a liquid collector installed between the reboiler and the column section. Experimental results in a φ 45mm batch column show that the proposed policy can overcome the flywheel effect caused by column liquid holdup and thus cut down operation time and energy consumption 31%-61%.
Keywords:batch distillation  slop cut  mode of operation  column holdup
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