萃取蒸馏
化学
共沸物
环己烷
环己烯
苯
共沸蒸馏
三元运算
三元数制
活度系数
再沸器
蒸馏
有机化学
热力学
催化作用
程序设计语言
水溶液
物理
相(物质)
计算机科学
作者
Wang Haiou,Yang Xu,Sang Weihe,Hao Li,Jing Fang
摘要
Abstract BACKGROUND Benzene, cyclohexane, and cyclohexene are ternary azeotropic systems, which cannot achieve high‐purity separation by ordinary distillation, but this issue can be solved by extractive distillation. Deep Eutectic Solvents (DES) is a ‘green solvent’ that has emerged in recent years and is often used as an extractant. RESULTS In this study, the COSMO‐SAC solvation model was used to calculate the infinite dilution activity coefficients (γ∞) of DES with different compositions to screen suitable DES, and the effect was demonstrated by vapor–liquid equilibrium experiment (VLE). In addition, the effect of intermolecular interactions was explored in this study by means of independent gradient (IGM) equivalence plot, and process simulations were carried out by means of Aspen Plus software. CONCLUSION VLE experiments showed that the combination of DES extractants tetrabutylphosphonium bromide: levulinic acid (1:4) and tetrabutylammonium bromide: cyclobutyl sulfone (1:4) could break the azeotropic relationship of benzene, cyclohexane, and cyclohexene ternary systems. In addition, using Aspen process simulation to compare the screened DES extractant with the industrially used dimethylacetamide (DMAC) extractant, the use of the screened DES extractant was able to reduce the condenser and reboiler energy consumption by 14.93%. © 2024 Society of Chemical Industry (SCI).
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