首页> 外文OA文献 >Liquid–Liquid, Vapor–Liquid, and Vapor–Liquid–Liquid Equilibrium Data for the Water–n-Butanol–Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation
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Liquid–Liquid, Vapor–Liquid, and Vapor–Liquid–Liquid Equilibrium Data for the Water–n-Butanol–Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation

机译:常压水-正丁醇-环己烷体系的液-液,汽-液和​​汽-液-液平衡数据:实验测定和相关性

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摘要

The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liquid equilibrium (VLE) of a ternary mixture of water–n-butanol–cyclohexane were measured at atmospheric pressure (101.32 kPa) in a modified dynamic recirculating still. As found in the literature, the experimental data obtained reveal a ternary azeotrope at 341.86 K with a mole fraction composition of 0.281, 0.034, and 0.685 water, n-butanol, and cyclohexane, respectively. The liquid–liquid equilibrium (LLE) compositions were measured at a constant temperature of 313.15 K and compared with data in the literature collected at other temperatures. Thermodynamic consistency of all the experimental data was demonstrated. The universal quasichemical (UNIQUAC) and the nonrandom two-liquid (NRTL) thermodynamic models were used to correlate the VLE and LLE data, while the original universal functional (UNIFAC) model was used to compare the predicted data.
机译:在大气压(101.32 kPa)下,以改进的动态特性测量了水-正丁醇-环己烷三元混合物的汽-液-液平衡(VLLE)和汽-液平衡(VLE)的温度和组成。仍在循环。如文献中所发现,获得的实验数据揭示了三元共沸物在341.86 K处的摩尔分数组成分别为水,正丁醇和环己烷的0.281、0.034和0.685。在313.15 K的恒定温度下测量液-液平衡(LLE)成分,并将其与在其他温度下收集的文献数据进行比较。证明了所有实验数据的热力学一致性。通用准化学(UNIQUAC)模型和非随机两液(NRTL)热力学模型用于关联VLE和LLE数据,而原始通用函数(UNIFAC)模型用于比较预测数据。

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