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

机译:二甲苯异丁醇与间二甲苯,邻二甲苯和对二甲苯在101.3 kPa时的汽液平衡

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摘要

Vapor-liquid equilibria were measured for binary systems of isobutanol with m-xylene, o-xylene, and p-xylene at 101.3 kPa using a recirculating still. Teh accuracy of experimental measurements was +-0.1 K in temperature, +-0.01 kPa in pressure, and +-0.001 in mole fraction. Teh results were determined to be thermodynamically consistent according to the point-to-point consistency and Wisniak tests. All the systems show moderate positive deviations from ideality. The data were correlated with five liquid-phase activity coefficient models (Margules, Van Laar, Wilson, NRTL UNIQUAC).
机译:使用循环釜在101.3 kPa下测量异丁醇与间二甲苯,邻二甲苯和对二甲苯的二元体系的汽液平衡。实验测量的准确度是温度为+ -0.1 K,压力为+ -0.01 kPa,摩尔分数为+ -0.001。根据点对点一致性和Wisniak测试,结果确定为热力学一致。所有系统都显示出与理想情况相差适中的正偏差。数据与五个液相活度系数模型(Margules,Van Laar,Wilson,NRTL UNIQUAC)相关。

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