首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Vapor-Phase Mole Fractions Determined from the P, x Data Using the Margules Equation for High-Pressure Binary Vapor-Liquid Equilibrium Systems Including Carbon Dioxide
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Vapor-Phase Mole Fractions Determined from the P, x Data Using the Margules Equation for High-Pressure Binary Vapor-Liquid Equilibrium Systems Including Carbon Dioxide

机译:使用Margules方程由P,x数据确定的气相二元分子分数,用于包含二氧化碳的高压二元气相-液相平衡系统

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摘要

High-pressure P, x data for CO2 + hydrocarbons, methanol, ethanol, and water binaries were correlated using the Margules equation. The average relative difference between experimental data and the correlation was as low as 1 % at T < T_(c1), where T and T_(c1) denote the system temperature and the critical temperature of the lighter component, It was found that the average relative difference of the vapor phase mole fractions from the Margules equation representing the P, x data is 0.6 % for the asymmetric and nonazeotropic binaries. A criterion for identifying the nonazeotropic binaries is proposed. The strength of molecular interactions and molecular order were identified for the azeotropic and zeotropic mixtures using partial molar excess enthalpies and entropies at infinite dilution. A method for the high-precision correlation of infinite dilution activity coefficients is proposed.
机译:使用Margules方程将CO2 +碳氢化合物,甲醇,乙醇和水的二元化合物的高压P,x数据关联起来。在T

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