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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Isobaric Vapor-Liquid Equilibria of the Binary Systems Cyclohexane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.3 kPa
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Isobaric Vapor-Liquid Equilibria of the Binary Systems Cyclohexane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.3 kPa

机译:二甲苯环己烷与邻二甲苯,间二甲苯,对二甲苯和乙苯在101.3 kPa时的等压蒸气-液体平衡

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摘要

Isobaric vapor-liquid equilibria were measured for cyclohexane + o-xylene, + m-xylene, + p-xylene, and + ethylbenzene at 101.3 kPa using a dynamic still with circulation of both phases. Experimental data were tested for thermodynamic consistency and satisfactorily correlated by different equations. The four systems exhibit positive deviations from ideal behavior. A comparative analysis was performed by application of the ASOG, original UNIFAC, modified UNIFAC (Dortmund), and modified UNIFAC (Lyngby) systems, and low root-mean-square deviations of vapor mole fraction and temperature were computed.
机译:使用两相循环的动态蒸馏仪,在101.3 kPa下测量了环己烷+邻二甲苯,+间二甲苯,+对二甲苯和+乙苯的等压蒸气-液体平衡。测试了实验数据的热力学一致性,并通过不同的方程式令人满意地进行了相关。这四个系统表现出与理想行为的正偏差。通过应用ASOG,原始UNIFAC,改进的UNIFAC(Dortmund)和改进的UNIFAC(Lyngby)系统进行比较分析,并计算出蒸汽摩尔分数和温度的均方根偏差低。

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