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甲醇-乙酸异戊酯、碳酸二甲酯-乙酸异戊酯和甲醇-1,2-丙二醇汽液平衡数据的测定与关联
引用本文:施云海,李文清,涂晋林.甲醇-乙酸异戊酯、碳酸二甲酯-乙酸异戊酯和甲醇-1,2-丙二醇汽液平衡数据的测定与关联[J].高校化学工程学报,1999(2).
作者姓名:施云海  李文清  涂晋林
作者单位:华东理工大学化学工程研究所!上海200237
基金项目:中国石化总公司科技开发部资助项目
摘    要:在Ellis平衡蒸馏器中测定了101.325kPa下甲醇(1)-乙酸异戊酯(2)、碳酸二甲酯(1)-乙酸异戊酯(2)和甲醇(1)-1,2-丙二醇(2)三对二元系的汽液相平衡数据。采用统计学方法对实验数据进行了热力学一致性校验。用改进的Peng-Robinson状态方程计算汽相的逸度系数,液相活度系数用Wilson和NRTL模型计算,对实验数据进行了关联。

关 键 词:汽液平衡  二元系  甲醇  乙酸异戊酯  碳酸二甲酯  1  2-丙二醇

Vapor-Liquid Equilibria for Binary Systems of Methanol-Isoamy Acetate, Dimethyl Carbonate-Isoamyl Acetate, and Methanol-1,2-Propanediol at 101.325kPa
Shi Yunhai, Li Wenqing, Tu Jinlin.Vapor-Liquid Equilibria for Binary Systems of Methanol-Isoamy Acetate, Dimethyl Carbonate-Isoamyl Acetate, and Methanol-1,2-Propanediol at 101.325kPa[J].Journal of Chemical Engineering of Chinese Universities,1999(2).
Authors:Shi Yunhai  Li Wenqing  Tu Jinlin
Abstract:The isobaric vapor-liquid equilibrium data for the binary systems of methanol(l)isoamyl acetate(2), dimethyl carbonate(1)-isoamyl acetate(2), and methanol(1 )- 1,2-propanediol(2) at101.325kPa are measured with an Ellis equilibrated distillator. Statistical method is applied to test thethermodynamic consistency. The experimental data can be satisfactorily correlated by the modifiedPeng-Robinson equation of state, which is applied to calculate fugacity coefficients for vapor phase,and Wilson and NRTL activity coefficient models, which are used to calculate activities for liquidphase.
Keywords:Vapor-liquid equilibrium  Binary system  Methanol  Dimethyl carbonate  Isoamylacetate  1  2-Propanediol
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