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丙酮-乙酸异丙烯酯二元体系常压汽液平衡
引用本文:王荣富,陈葵,朱家文,武斌.丙酮-乙酸异丙烯酯二元体系常压汽液平衡[J].化学工业与工程,2007,24(3):262-265.
作者姓名:王荣富  陈葵  朱家文  武斌
作者单位:华东理工大学化工学院,上海,200237
摘    要:用改进的埃利斯(Ellis)平衡蒸馏器测定了丙酮-乙酸异丙烯酯二元系统在常压下的汽液平衡数据,用液相活度模型Wilson、NRTL方程对测定数据进行关联,采用非线性最小二乘法回归出二元系统在常压下的Wilson、NRTL方程参数,Wilson模型与试验值符合良好.汽液相平衡数据经Herrington面积法检验满足热力学一致性.

关 键 词:丙酮  乙酸异丙烯酯  汽液平衡  参数回归  丙酮  乙酸异丙烯酯  二元体系  汽液平衡  Binary  System  Acetate  Equilibrium  一致性  热力学  检验  面积法  相平衡数据  试验  活度模型  参数  回归  乘法  最小  非线性  关联
文章编号:1004-9533(2007)03-0262-04
收稿时间:2006-04-13
修稿时间:2006年4月13日

Atmospheric Vapor-Liquid Equilibrium of Acetone-Isopropenyl Acetate Binary System
WANG Rong-fu,CHEN Kui,ZHU Jia-wen,WU Bin.Atmospheric Vapor-Liquid Equilibrium of Acetone-Isopropenyl Acetate Binary System[J].Chemical Industry and Engineering,2007,24(3):262-265.
Authors:WANG Rong-fu  CHEN Kui  ZHU Jia-wen  WU Bin
Affiliation:College of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China
Abstract:The atmospheric vapor-liquid equilibrium(VLE) data of acetone-isopropenyl acetate binary system were measured by using the improved Ellis equilibrium distiller.Thermodynamic calculation of the experimental data were carried out by using ideal equation for gas phase and using NRTL and Wilson equation for liquid phase.The parameters of NRTL and Wilson model for this binary system were regressed by nonlinear least square method,and the calculated data from Wilson model accorded well with the experimental data.The VLE data were tested by Herrington method and showed satisfying thermodynamic consistency.
Keywords:acetone  isopropenyl acetate  vapor-liquid equilibrium(VLE)  parameters regression
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