...
首页> 外文期刊>Fluid Phase Equilibria >Vapor-liquid equilibria and density measurement for binary mixtures of o-xylene plus NMF, m-xylene plus NMF and p-xylene + NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
【24h】

Vapor-liquid equilibria and density measurement for binary mixtures of o-xylene plus NMF, m-xylene plus NMF and p-xylene + NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa

机译:从0 kPa到101.3 kPa在333.15 K,343.15 K和353.15 K上邻二甲苯+ NMF,间二甲苯+ NMF和对二甲苯+ NMF的二元混合物的汽液平衡和密度测量

获取原文
获取原文并翻译 | 示例

摘要

Isothermal vapor-liquid equilibria at 333.15 K, 343.15 K and 353.15 K for three binary mixtures of o-xylene, m-xylene and p-xylene individually mixed with N-methylformamide (NMF), have been obtained at pressures ranged from 0 kPa to 101.3 kPa over the whole composition range. The Wilson, NRTL and UNIQUAC activity coefficient models have been employed to correlate experimental pressures and liquid mole fractions. The non-ideal behavior of the vapor phase has been considered by using the Peng-Robinson equation of state in calculating the vapor mole fraction. Liquid and vapor densities were measured by using two vibrating tube densitometers. The excess molar volumes of the liquid phase were also determined. Three systems of o-xylene + NMF. m-xylene + NMF and p-xylene + NMF mixtures present large positive deviations from the ideal solution and belong to endothermic mixings because their excess Gibbs energies are positive. Temperature dependent intermolecular parameters in the NRTL model correlation were finally obtained in this study.
机译:在压力范围为0 kPa至0kPa至在整个组成范围内为101.3 kPa。 Wilson,NRTL和UNIQUAC活度系数模型已用于关联实验压力和液体摩尔分数。在计算蒸气摩尔分数时,已通过使用Peng-Robinson状态方程考虑了蒸气相的非理想行为。通过使用两个振动管密度计测量液体和蒸气密度。还确定了液相的过量摩尔体积。邻二甲苯+ NMF的三种体系。间二甲苯+ NMF和对二甲苯+ NMF混合物与理想溶液存在较大的正偏差,属于吸热混合,因为它们的过量吉布斯能量为正。在这项研究中,最终获得了与温度相关的分子间参数,它们与NRTL模型相关。

著录项

相似文献

  • 外文文献
  • 中文文献
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号