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离子液体萃取精馏分离甲醇-乙腈共沸体系

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使用离子液体 1-己基-3-甲基咪唑六氟磷酸盐([HMIM][PF6])作为分离甲醇和乙腈共沸物系的夹带剂,在101.3 kPa下获得了三元气液相平衡(VLE)数据,用非随机双液(NRTL)模型关联实验数据,得到基于 NRTL 模型的二元交互作用参数,同时计算出离子液体打破共沸需要的最小摩尔分数为0.036 7.最后,用过量焓分析解释分离机理.
Separation of Methanol-Acetonitrile Azeotrope System by Ionic Liquid Extractive Distillation
The ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate([HMIM][PF6])was used as the entrainer for separating the azeotrope system of methanol and acetonitrile.The ternary vapor-liquid equilibrium(VLE)data were obtained at 101.3 kPa.The experimental data were correlated with the non-random dual-liquid(NRTL)model to obtain the binary interaction parameters.At the same time,the minimum mole fraction required to break the azeotrope was calculated to be 0.036 7.The separation mechanism was explained by excess enthalpy analysis.

MethanolAcetonitrileIonic liquidNRTLExcess enthalpy analysis

李丽、肖孟杰、李文秀、马帅、张弢

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沈阳化工大学 辽宁省化工分离技术重点实验室,辽宁 沈阳 110142

甲醇 乙腈 离子液体 NRTL 过量焓分析

国家自然科学基金

21576166

2024

辽宁化工
辽宁省化工学会

辽宁化工

影响因子:0.234
ISSN:1004-0935
年,卷(期):2024.53(5)
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