首页|基于Aspen的乙酸乙酯-乙醇-水体系恒沸精馏和萃取精馏模拟

基于Aspen的乙酸乙酯-乙醇-水体系恒沸精馏和萃取精馏模拟

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利用Aspen Plus软件模拟乙酸乙酯-乙醇-水体系先恒沸精馏,再用水作为萃取剂,通过三次萃取精馏,最终得到质量分数大于99.5%乙酸乙酯成品,总回收率约89%~90%,萃取剂通过提馏塔提纯,循环使用.研究思路和方法适用于二元或三元共沸物体系的精馏提纯.
Simulation of Azeotropic Distillation and Extractive Distillation of Ethyl Acetate-Ethanol-Water System based on Aspen
This paper uses Aspen Plus software to simulate the azeotropic distillation of ethyl acetate-ethanol-water system,followed by water as the extractant.Through three rounds of extraction distillation,the final product of ethyl acetate with a mass fraction greater than 99.5%is obtained,with a total recovery rate of about 89%~90%.The extractant is purified through the distillation column and recycled.The research ideas and methods are applicable to the distillation purification of binary or ternary azeotrope systems.

aspenethyl acetateazeotropic distillationextractive distillation

葛仁祥

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安道麦辉丰(江苏)有限公司,江苏盐城 224100

Aspen 乙酸乙酯 恒沸精馏 萃取精馏

2024

化工设计
中国成达工程有限公司 中国石油和化工勘察设计协会

化工设计

影响因子:0.262
ISSN:1007-6247
年,卷(期):2024.34(3)