非随机双液模型
化学
等压法
共沸物
汽液平衡
乙二醇
蒸汽压
活度系数
热力学
色谱法
蒸馏
有机化学
水溶液
物理
作者
Feihu Li,Mengyuan Li,Guo Jin,Xiwei Hu,Jiaming Zhu,Qunsheng Li,Hongkang Zhao
标识
DOI:10.1021/acs.jced.2c00609
摘要
N-Propanol (NPA) and n-propyl acetate (NPAC) can form an azeotrope under normal pressure, so their separation cannot be carried out by conventional distillation. Therefore, 1-butyl-3-methylimidazole acetate ([BMIM][OAC]) and ethylene glycol (EG) were selected as entrainers for extractive distillation of the two substances. Isobaric vapor–liquid equilibrium data were obtained by experiments of NPA + NPAC, NPA + NPAC + [BMIM][OAC], and NPA + NPAC + EG at normal pressure; the experimental results showed that the separation effect of [BMIM][OAC] is significantly better than that of EG. Finally, the data were fitted and correlated with the NRTL model. The ARD (average relative deviation) of NPA + NPAC, NPA + NPAC + [BMIM][OAC], and NPA + NPAC + EG is less than 5%, indicating that the NRTL model has good applicability to the vapor–liquid system.
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