首页> 外文期刊>Fluid Phase Equilibria >Experimental isobaric vapour-liquid-liquid equilibrium data for the quaternary systems water (1)-ethanol and water (1)-ethanol (2)-acetone (3)-n-butyl acetate (4) (2)-acetone (3)-methyl ethyl ketone (4) and their partially miscible-constituent ternar
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Experimental isobaric vapour-liquid-liquid equilibrium data for the quaternary systems water (1)-ethanol and water (1)-ethanol (2)-acetone (3)-n-butyl acetate (4) (2)-acetone (3)-methyl ethyl ketone (4) and their partially miscible-constituent ternar

机译:四元体系水(1)-乙醇和水(1)-乙醇(2)-丙酮(3)-乙酸正丁酯(4)(2)-丙酮(3)的实验等压蒸气-液-液平衡数据-甲乙酮(4)及其部分可混溶的叔丁基

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Experimental vapour-liquid-liquid equilibrium data for the (type B) quaternary systems water (1)-ethanol (2)-acetone (3)-n-butyl acetate (4) and water (I)-ethanol (2)-acetone (3)-methyl ethyl ketone (4) were measured using a circulation equilibrium still employing vigorous mechanical mixing in the boiling chamber. The first quaternary system was measured isobarically at pressures of 760, 600 and 360 mm Hg, and the other system measured isobarically at atmospheric pressure. The partially miscible constituent ternaries of both quaternary systems, water (1)-acetone (2)-n-butyl acetate (3), water (1)-ethanol (2)-n-butyl acetate (3), water (1)-acetone (2)-methyl ethyl ketone (3) and water (I)-ethanol (2)-methyl ethyl ketone (3) were also measured at the same conditions. The measured experimental data were found to be thermodynamically consistent according to the isobaric point-by-point thermodynamic consistency criterion of Wisniak. (c) 2006 Elsevier B.V. All rights reserved.
机译:(B型)季体系水(1)-乙醇(2)-丙酮(3)-乙酸正丁酯(4)和水(I)-乙醇(2)-丙酮的实验蒸气-液-液平衡数据(3)-甲基乙基酮(4)使用仍然在沸腾室中进行剧烈机械混合的循环平衡来测量。第一个四元系统在760、600和360 mm Hg的压力下等压测量,而另一个系统在大气压下等压测量。两个四元体系的部分可混溶的三元组分,水(1)-丙酮(2)-乙酸正丁酯(3),水(1)-乙醇(2)-乙酸正丁酯(3),水(1)还在相同条件下测量了-丙酮(2)-甲基乙基酮(3)和水(I)-乙醇(2)-甲基乙基酮(3)。根据Wisniak的等压点对点热力学一致性判据,测得的实验数据具有热力学一致性。 (c)2006 Elsevier B.V.保留所有权利。

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