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摘要
甲醇-四氢呋喃属于共沸体系,传统分离工艺采用双塔串联萃取工艺进行分离纯化,即引入第三种组分,该工艺能耗、占地面积等相对较高。该研究尝试提出了一种新的工艺方法,即热耦萃取分离工艺(精馏工艺与萃取工艺相耦合);对相关工艺参数进行优化设计分析,得到最佳操作参数;与传统双塔萃取工艺相比,热耦萃取工艺可减少能耗约5%,同时设备投资及占地面积也相应减少。
Abstract
Methanol-tetrahydrofuran azeotropic system is traditionally separated and purified by two-column series extraction process,in which the third component is used.Such a traditional process consumes relatively high energy and occupies large land area.This study proposes a new separation process for separation of methanol-tetrahydrofuran azeotropic system,named thermal-coupled extraction separation process which integrating distillation process and extraction process.The optimum operation parameters are determined through optimization design analysis.Compared with traditional process,this thermal-coupled extraction distillation process can save energy by about 5% and cut down capital investment,and needs smaller land area.
关键词
共沸
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节能
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操作参数
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优化
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热耦精馏
Key words
azeotropic system
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energy-saving
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operation parameters
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optimization
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thermal-coupled extraction distillation process
Author summay
郝增华(1980-),女,硕士,讲师,hgr2018@126.com
热耦萃取精馏分离应用于甲醇-四氢呋喃体系的优化设计分析[J].
现代化工, 2020, 40(9): 194-197 DOI:10.16606/j.cnki.issn0253-4320.2020.09.040