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首页> 外文期刊>Fluid Phase Equilibria >Phase equilibrium for the binary azeotropic mixture of trifluoroiodomethane (R13I1)+1,1,2,2-tetrafluoroethane (R134) at temperatures from 258.150 to 283.150K
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Phase equilibrium for the binary azeotropic mixture of trifluoroiodomethane (R13I1)+1,1,2,2-tetrafluoroethane (R134) at temperatures from 258.150 to 283.150K

机译:三氟碘甲烷(R13I1)+ 1,1,2,2-四氟乙烷(R134)的二元共沸混合物的相平衡在258.150至283.150K的温度下

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摘要

Isothermal vapor-liquid equilibrium data of binary trifluoroiodomethane (R13I1) + 1,1,2,2-tetrafluoroethane (R134) systems at 258.150, 263.150, 273.150 and 283.150. K were measured by a recirculation apparatus with visual windows. The measured uncertainties of the temperature, pressure, and compositions are less than ±5. mK, ±0.0005. MPa, and ±0.005, respectively. All the experimental data were correlated by the Peng-Robinson (PR) EoS with the Huron-Vidal (HV) mixing rule utilizing the non-random two-liquid (NRTL) activity coefficient model. Azeotropic behavior can be found at the measured temperature range.
机译:二元三氟碘甲烷(R13I1)+ 1,1,2,2-四氟乙烷(R134)系统的等温气液平衡数据分别为258.150、263.150、273.150和283.150。通过具有可视窗口的再循环设备测量K。测得的温度,压力和组成的不确定度小于±5。 mK,±0.0005。 MPa和±0.005,分别。使用非随机二液(NRTL)活性系数模型,通过Peng-Robinson(PR)EoS与Huron-Vidal(HV)混合规则关联所有实验数据。共沸行为可以在测得的温度范围内找到。

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