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双效精馏精制甲缩醛的过程模拟

段继海 任晓晗 王伟文

化学工程Issue(6):69-73,5.
化学工程Issue(6):69-73,5.DOI:10.3969/j.issn.1005-9954.2014.06.015

双效精馏精制甲缩醛的过程模拟

Simulation of double-effect distillation separation of methylal

段继海 1任晓晗 1王伟文1

作者信息

  • 1. 青岛科技大学 化工学院,山东 青岛 266061
  • 折叠

摘要

Abstract

In the process of manufacturing highly-concentrated aqueous formaldehyde solution by methylal oxidation, when concentrated methylal is distillated,it is easy to form a methanol-methylal azeotropic system,and difficult to obtain high-purity methylal.The methanol-methylal azeotropic composition changes with pressure,thus many existing processes use swing-pressure distillation (using high-pressure column)to separate methylal.There are many disadvantages,such as high energy consumption and low efficiency,which result in great energy loss.To improve the efficiency of the tower,the process of separating methylal was improved by combining swing-pressure distillation with double-effect distillation.The simulation results are as follows:the high pressure column is built up by 27 theoretical plates,the pressure is 1 000 kPa,the energy saving rates of the bottom reboiler in the double-effect distillation process is 54.97%,and the energy saving rates of the overhead condenser is 37.79%.

关键词

甲缩醛/Aspen Plus模拟/双效精馏

Key words

methylal/Aspen Plus simulation/double-effect distillation

分类

化学化工

引用本文复制引用

段继海,任晓晗,王伟文..双效精馏精制甲缩醛的过程模拟[J].化学工程,2014,(6):69-73,5.

基金项目

国家自然科学基金资助项目(21276132);山东省博士基金项目 ()

化学工程

OA北大核心CSCDCSTPCD

1005-9954

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