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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 for binary systems of acetone plus isopropenyl acetate, 2-butanone plus isopropenyl acetate, and isopropenyl acetate plus acetylacetone at 101.3 kPa
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Isobaric vapor-liquid equilibria for binary systems of acetone plus isopropenyl acetate, 2-butanone plus isopropenyl acetate, and isopropenyl acetate plus acetylacetone at 101.3 kPa

机译:丙酮加乙酸异丙烯酯,2-丁酮加乙酸异丙烯酯和乙酸异丙烯酯加乙酰丙酮的二元体系的等压蒸气-液体平衡

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摘要

Isobaric vapor-liquid equilibrium (VLE) data have been determined with a circulation still at 101.3 kPa for binary systems of acetone + isopropenyl acetate, 2-butanone + isopropenyl acetate, and isopropenyl acetate + acetylacetone. No azeotropic behavior was found in any of the systems studied. Thermodynamic consistency has been tested for all VLE data. The experimental data have been correlated satisfactorily by the NRTL, UNIQUAC, and Wilson models. Predictions by using group-contribution methods, such as the original UNIFAC, UNIFAC-Dortmund, and UNIFAC-Lyngby, have been compared with the experimental results.
机译:对于丙酮+乙酸异丙烯酯,2-丁酮+乙酸异丙烯酯和乙酸异丙烯酯+乙酰丙酮的二元体系,仍在101.3 kPa的循环条件下确定了等压气液平衡(VLE)数据。在所研究的任何系统中均未发现共沸行为。已对所有VLE数据进行了热力学一致性测试。通过NRTL,UNIQUAC和Wilson模型令人满意地关联了实验数据。使用组贡献方法(例如原始的UNIFAC,UNIFAC-Dortmund和UNIFAC-Lyngby)进行的预测已与实验结果进行了比较。

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