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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Phase Equilibria of HFC Mixtures: Binary Mixtures of Trifluoromethane + 1,1-Difluoroethane and Trifluoromethane + 1,1,1-Trifluoroethane at 283.15 and 293.15 K
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Phase Equilibria of HFC Mixtures: Binary Mixtures of Trifluoromethane + 1,1-Difluoroethane and Trifluoromethane + 1,1,1-Trifluoroethane at 283.15 and 293.15 K

机译:HFC混合物的相平衡:三氟甲烷+ 1,1-二氟乙烷和三氟甲烷+ 1,1,1-三氟乙烷的二元混合物在283.15和293.15 K

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Isothermal vapor-liquid equilibria for the binary mixtures of trifluoromethane (R-23) + 1,1-difluoroethane (HFC-152a) and trifluoromethane + 1,1,1-trifluoroethane (HFC-143a) were measured at 283.15 and 293.15 K. The experiments were carried out witha circulation-type equilibrium apparatus with the measurement of temperature, pressure, and the compositions of the liquid and vapor phases. The experimental data were correlated with the Peng-Robinson equationof state using the Wong andSandler mixing rules and the Carnahan-Starling-Desantis(CSD) equation of state. Calculated results with these equations showed good agreement witht he experimental data, but the Peng-Robinson equation of state gave more accurate predictions for the binary systems.Azeotropic behavior has not been found in either of these mixtures.
机译:在283.15和293.15 K下测量了三氟甲烷(R-23)+ 1,1-二氟乙烷(HFC-152a)和三氟甲烷+ 1,1,1-三氟乙烷(HFC-143a)二元混合物的等温气液平衡。用循环型平衡装置进行实验,测量温度,压力以及液相和气相的组成。使用Wong和Sandler混合规则以及Carnahan-Starling-Desantis(CSD)状态方程,将实验数据与Peng-Robinson状态方程相关。这些方程的计算结果与实验数据吻合良好,但是Peng-Robinson状态方程对二元体系的预测更为准确。在这两种混合物中均未发现共沸行为。

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