详细信息
乙二醇、二甘醇对醇-水萃取精馏影响的数模计算与验证 ( EI收录)
Mathematical Modelling and Identification in Extractive Distillation of Alcohol-Water with Glycol and Diethylene Glycol
文献类型:期刊文献
中文题名:乙二醇、二甘醇对醇-水萃取精馏影响的数模计算与验证
英文题名:Mathematical Modelling and Identification in Extractive Distillation of Alcohol-Water with Glycol and Diethylene Glycol
作者:刘凡[1];黄福江[1];张翠华[1];张成芳[1]
机构:[1]华东化工学院化学工程系
年份:1993
卷号:19
期号:3
起止页码:254
中文期刊名:华东化工学院学报
外文期刊名:Huadong Huagong Xueyuan Xuebao/Journal of East China Institute of Chemical Technology
收录:国家哲学社会科学学术期刊数据库;EI(收录号:1994061321925);Scopus;CSCD:【CSCD2011_2012】;
语种:中文
中文关键词:醇;萃取;精馏;乙二醇;二甘醇
外文关键词:mixed alcohols;separation of extractive distillation;alcohol-water separation;multicomponent vapour-liquid equilibrium
摘要:应用多元汽液相平衡原理进行了乙二醇、二甘醇对醇-水萃取精馏影响的数模计算,并予以实验验证。模型计算值与实验值的最大误差△Y≤0.030,认为Wilson模型对醇-水物系是合宜的;乙二醇、二甘醇是醇-水萃取精馏分离的两种较好的萃取剂。
The principle of multicomponent vapour-liquid equilibrium was applied in mathematical modelling of extractive distillation for alcohol-water systems with glycol and diethylene glycol. They were identified with experimental results. The maximum deviation value of calculation and experimental is △y=0.030. It was concluded that Wilson's model is considered to be suitable for alcohol-water system; Both glycol and diethylene glycol are good extraciants for alcohol and water separation by extractive distillation.
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