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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Vapor-Liquid Equilibria for the Ternary System Acetone + Methanol + Water at 101.325 kPa
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Vapor-Liquid Equilibria for the Ternary System Acetone + Methanol + Water at 101.325 kPa

机译:三元体系丙酮+甲醇+水在101.325 kPa时的汽液平衡

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摘要

The vapor-liquid equilibrium at 101.325 kPa has been measured for the ternary system acetone + methanol + water in an equilibrium still with circulation of phases. Satisfactory results were obtained for the prediction of activity coefficients and the equilibrium compositions iwht group contribution models (ASOG, UNIFAC, UNIFAC-Dortmund, and UNIFAC-Lyngby). Small standard deviations of vapor molar fraction and temperature were calculated. azeotropic behavior was observed only in the acetone + methanol mixture. The correlation parameters for the Tamir-Wisniak and UNIQUAC equations were presented.
机译:对于三元体系丙酮+甲醇+水,在相平衡的平衡下仍测量了101.325 kPa的气液平衡。对于群体贡献模型(ASOG,UNIFAC,UNIFAC-Dortmund和UNIFAC-Lyngby)的活动系数和平衡组成的预测,均获得了令人满意的结果。计算出蒸气摩尔分数和温度的小标准偏差。仅在丙酮+甲醇混合物中观察到共沸行为。给出了Tamir-Wisniak方程和UNIQUAC方程的相关参数。

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