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首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Liquid-Liquid Equilibria for Ternary Systems of (Ethyl Methyl Carbonate plus Methanol or Ethanol plus Water) at 293.15, 303.15, and 308.15 K
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Liquid-Liquid Equilibria for Ternary Systems of (Ethyl Methyl Carbonate plus Methanol or Ethanol plus Water) at 293.15, 303.15, and 308.15 K

机译:用于293.15,303.15和308.15 k的(乙基碳酸甲酯加甲醇或乙醇加水)的三元系统的液液平衡

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摘要

Liquid-phase composition values for {water + methanol + ethyl methyl carbonate (EMC)} and (water + ethanol + EMC) were determined at temperatures of 293.15, 303.15, and 308.15 K at 101 kPa. Thermodynamic modified UNIQUAC and extended UNIQUAC models were used in regression of the experimental values, with average root mean -square deviations of 0.96 and 1.45% in mole fraction, respectively. Moreover, optimum binary interaction parameters of (methanol or ethanol + EMC) were obtained by regression analysis of the phase composition values. The experimental data consistency was further ascertained by applying the Bachman equation. Distribution coefficients and separation factors were used to assess the extraction performance of EMC in the separation of methanol and ethanol from water.
机译:{水+甲醇+碳酸甲酯(EMC)}和(水+乙醇+ EMC)的液相成分值在101kPa的温度下在293.15,303.15和308.15k的温度下测定。 热力学改性的uniquac和扩展的uniquac模型用于实验值的回归,平均根部平均值分别为0.96和1.45%的偏离偏差。 此外,通过对相组成值的回归分析获得(甲醇或乙醇+ EMC)的最佳二元相互作用参数。 通过应用Bachman方程,进一步确定了实验数据一致性。 分配系数和分离因子用于评估EMC在水中分离水中的提取性能和水中的乙醇。

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