首页> 外文期刊>Journal of Chemical and Engineering Data: the ACS Journal for Data >Phase equilibria of the binary systems 1-hexene with o-xylene, m-xylene, p-xylene, toluene, and ethylbenzene at 101.3 kPa
【24h】

Phase equilibria of the binary systems 1-hexene with o-xylene, m-xylene, p-xylene, toluene, and ethylbenzene at 101.3 kPa

机译:在101.3 kPa下1-己烯与邻二甲苯,间二甲苯,对二甲苯,甲苯和乙苯的二元体系的相平衡

获取原文
获取原文并翻译 | 示例
获取外文期刊封面目录资料

摘要

Isobaric vapor-liquid equilibria are measured for 1-hexene + o-xylene, + m-xylene, + p-xylene, + toluene, and + ethylbenzene at 101.3 kPa, using a dynamic still with circulation in both of the phases. The experimental data are tested for thermodynamic consistency and could be represented well by the Wilson and UNIQUAC equations, with the latter being far better. A comparative analysis of the application of the group contribution methods ASOG, original UNIFAC, modified UNIFAC-Dortmund, and modified UNIFAC-Lyngby to the mixtures of this study showed that UNIFAC-Lyngby gives better results. [References: 26]
机译:使用动态蒸馏器在两个相中循环,在101.3 kPa下测量1-己烯+邻二甲苯,+间二甲苯,+对二甲苯,+甲苯和+乙苯的等压蒸气-液体平衡。实验数据经过热力学一致性测试,可以用Wilson和UNIQUAC方程很好地表示,后者要好得多。对组贡献方法ASOG,原始UNIFAC,改良的UNIFAC-Dortmund和改良的UNIFAC-Lyngby在本研究混合物中的应用进行比较分析,结果表明UNIFAC-Lyngby给出了更好的结果。 [参考:26]

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
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