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首页> 外文期刊>The Korean journal of chemical engineering >Vapor-liquid equilibria for the binary mixtures of dimethyl ether (DME) plus dimethyl carbonate (DMC)
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Vapor-liquid equilibria for the binary mixtures of dimethyl ether (DME) plus dimethyl carbonate (DMC)

机译:二甲醚(DME)和碳酸二甲酯(DMC)的二元混合物的汽液平衡

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摘要

Isothermal vapor-liquid equilibrium data for the binary system of dimethyl ether (DME)+ dimethyl carbonate (DMC) were measured at 303.15, 313.15, 323.15, 333.15 and 343.15 K using a circulation-type equilibrium apparatus with on-line gas chromatography analysis. The experimental data were correlated with the Peng-Robinson equation of state (PR-EoS) using the van der Waals one fluid mixing rule and the Peng-Robinson equation of state (PR-EoS) using the Wong-Sandler mixing rule combined with the NRTL excess Gibbs free energy model. This system showed negative deviation from Raoult's law, and no azeotropic behavior was observed for all the temperature ranges studied here. Calculated results with PR-EoS using both two mixing rules showed good agreement with experimental data.
机译:使用带有在线气相色谱分析的循环式平衡装置,在303.15、313.15、323.15、333.15和343.15 K下测量了二甲醚(DME)+碳酸二甲酯(DMC)二元系统的等温气液平衡数据。使用范德华斯一流体混合法则将实验数据与Peng-Robinson状态方程(PR-EoS)和使用Wong-Sandler混合法则结合的Peng-Robinson状态方程(PR-EoS)相关联NRTL过剩的吉布斯自由能模型。该系统显示出与拉乌尔定律的负偏差,并且在此研究的所有温度范围内均未观察到共沸行为。使用两种混合规则的PR-EoS计算结果与实验数据吻合良好。

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