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首页> 外文期刊>Physics and Chemistry of Liquids >Isobaric vapor-liquid equilibria and densities for the binary systems oxolane + ethyl 1,1-dimethylethyl ether, oxolane + 2-propanol and propan-2-one + trichloromethane
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Isobaric vapor-liquid equilibria and densities for the binary systems oxolane + ethyl 1,1-dimethylethyl ether, oxolane + 2-propanol and propan-2-one + trichloromethane

机译:二元体系氧戊烷+ 1,1,1-二甲基乙基醚,氧戊烷+ 2-丙醇和丙-2-酮+三氯甲烷的等压蒸气-液体平衡和密度

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摘要

Vapor-liquid equilibrium data have been determined at 50 kPa for the binary systems oxolane (THF) + ethyl 1,1-dimethylethyl ether (ETBE) and oxolane + 2-propanol and at 94 kPa for the system propan-2-one + trichloromethane. excess volumes have also been determined from density measurements at 298.15K. The systems oxolane + ethyl 1,1-dimethylethyl ether and oxolane + 2-propanol exhibit slight to moderate positive deviations from ideal behavior and no azeotrope is present. The system propan-2-one + trichloromethane exhibits negative deviations from ideal behavior and presents an azeotrope. The excess volumes of the system oxolane + ethyl 1,1-dimethylethyl ether are negative over the whole mole fraction range while those of the system oxolane + 2-propanol are positive. Excess volumes of the system propan-2-one + trichloromethane, change from negative to positive as the concentration of propan-2-one increases. The activity coefficients and boiling points of the solutions were correlated with the mole fraction by the Wohl, Wilson, UNIQUAC, and NRTL equations, and predicted by the UNIFAC group contribution method. Excess volume data were correlated using the Redich-Kister expansion. The chemical association theory was applied for explaining the equilibrium behavior of the systems oxolane + 2-propanol and propan-2-one + trichloromethane.
机译:对于二元系统恶戊烷(THF)+乙基1,1-二甲基乙基醚(ETBE)和恶唑烷+ 2-丙醇,汽液平衡数据已确定为50 kPa,对于丙-2-酮+三氯甲烷系统已确定为94 kPa 。还通过298.15K的密度测量确定了多余的体积。环氧丙烷+乙基1,1-二甲基乙基醚和环氧丙烷+ 2-丙醇的体系与理想行为之间存在轻微至中度的正偏差,并且不存在共沸物。丙-2-酮+三氯甲烷系统显示出与理想行为的负偏差,并呈现共沸物。在整个摩尔分数范围内,系统环氧丙烷+ 1,1-二甲基乙基醚的过量体积为负,而系统环氧丙烷+ 2-丙醇的过量体积为正。随着丙-2-酮浓度的增加,系统中丙-2-酮+三氯甲烷的过量体积从负变为正。溶液的活度系数和沸点通过Wohl,Wilson,UNIQUAC和NRTL方程与摩尔分数相关,并通过UNIFAC基团贡献法进行预测。使用Redich-Kister扩展将过量的数据关联起来。应用化学缔合理论解释了环氧丙烷+ 2-丙醇和丙-2-酮+三氯甲烷体系的平衡行为。

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