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Vapour-Liquid Phase Equilibrium for CO2 + 2-Pentanol at Elevated Pressure

机译:高压下CO2 + 2-戊醇的气液相平衡

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Vapour-liquid phase equilibrium data for CO2 + 2-pentanol were measured at temperatures of 313.4, 333.5, 343.5 and 353.4 K in the pressure range of 4.88 to 13.51 MPa.The measurements were carried out in a variable-volume visual high-pressure cell. The experimental data were well correlated with Peng-Robinson equation of state (PR-EOS) together with van der Waals-2 mixing rule. Henry's constants and partial molar volumes of CO2 at infinite dilution were estimated with Kriehevsky-Kasamovsky equation.
机译:在压力为4.88至13.51 MPa的温度下,分别在313.4、333.5、343.5和353.4 K的温度下测量了CO2 + 2-戊醇的汽液相平衡数据。 。实验数据与Peng-Robinson状态方程(PR-EOS)以及van der Waals-2混合规则密切相关。用Kriehevsky-Kasamovsky方程估算无限稀释时的Henry常数和部分CO2摩尔体积。

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