醋酸甲酯
化学
甲醇
非随机双液模型
共沸物
等压法
相对波动率
三元运算
离子液体
乙酸乙酯
无机化学
波动性(金融)
乙酸丁酯
活度系数
有机化学
三元数制
汽液平衡
色谱法
UNIFAC公司
热力学
作者
Huaiwen Fan,Huiqin Zhou,Zhe Wu,Yongbo Chen,Qunsheng Li,Hongkang Zhao
标识
DOI:10.1021/acs.jced.6c00110
摘要
The isobaric vapor–liquid equilibrium experiments for the methyl acetate + methanol + ionic liquids (ILs) system were conducted at atmospheric pressure, with 1-butyl-3-methylimidazolium acetate ([BMIM][Ac]), 1-ethyl-3-methylimidazolium acetate ([EMIM][Ac]), and 1-ethyl-3-methylimidazolium dimethyl phosphate ([EMIM][DMP]) employed as entrainers. The ILs exhibit a significant salting-out effect on methyl acetate, resulting in a substantial increase in the relative volatility of methyl acetate with respect to that of methanol. The results show that all three extractants could effectively break the azeotrope of methyl acetate + methanol. The NRTL model was selected to correlate the experimental data, yielding an average relative deviation (ARD) of 3.19% for the binary methyl acetate + methanol system. For the ternary systems of methyl acetate + methanol + [BMIM][Ac], methyl acetate + methanol + [EMIM][Ac], and methyl acetate + methanol + [EMIM][DMP], the ARDs were 1.53%, 4.10%, and 4.04%, respectively, which indicates the good applicability of the NRTL model for the investigated systems.
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