期刊文献+
任意字段
题名或关键词
题名
关键词
文摘
作者
第一作者
机构
刊名
分类号
参考文献
作者简介
基金资助
栏目信息

活度系数模型预测汽-液相平衡的发展概况 被引量：2

Development on Prediction of VLE with Activity Coefficient Model
在线阅读 下载PDF
导出
摘要 本文综述了活度系数模型在预测汽-液相平衡方面的进展情况,特别对状态方程-超额吉布斯自由能模型(EOS-gE模型)的性能进行了详细分析,同时对各类模型的特点和适应范围也进行了简要的概括。 The development on prediction of vapour-liquid equilibrium（VLE） with activity coefficient model is described, and the equation of state / excess Gibbs free energy model （EOS-g^E） are commented in detail especially, also, their characteristics and applicability scope are briefly presented in this paper.
作者 傅杨武 王裕玲 陈书鸿
机构地区 重庆三峡学院化学与环境工程系
出处 《重庆三峡学院学报》 2006年第3期75-77,共3页 Journal of Chongqing Three Gorges University
基金 重庆市科委自然科学基金(CSTC 2005EA7037) 万州区科委重点科学技术项目[2005]3号
关键词 活度系数模型 汽液平衡 EOS-g^E模型 activity coefficient model, vapor-liquid equilibrium, EOS-gE model
分类号 TQ013.1 [化学工程]
  • 相关文献

参考文献8

  • 1Geprgios M.K,Panayiotis M.V.An interpretation of the behavior of EoS-GE models for asymmetric systems[J].Chemical Engineering Science,2000,55:2351-2358.
  • 2Huron M J,Vidal J.New mixing rules in simple EOS for representing VLE of strongly nonideal mixtures[J].Fluid Phase Equibria,1979,3:255-259.
  • 3Lermite C,Vidal J.A group contributioo equation of state for polar and non-polar compounds[J].Fluid Phase Equibria.1992,72:111-130.
  • 4Michelsen M J.A Method for incorporating excess Gibbs energy models in equation of state.Fluid Phase Equibria[J],1990,60:213.
  • 5Holderbaum T,Gmehling J.PSRK:A Group Contribution Equation of State Based on UNIFAC[J].Fluid Phase Equibria,1991,70:251-265.
  • 6Jiding Li,Fischer K,Gmehling J.Prediction of vapor-liquid for asymmetric systems at low and high pressure with the PSRK model[J].Fluid Phase Equilibria,1998,143:71-82.
  • 7Spiliotis N M,Boukouvalas Ch,Tassios D P.The modelsi-MHV1 and LCVM:prediction of phase equilibria in multicompo-nent systems[J].First Greek Chemical Engineering Conference,1997,31:325-330.
  • 8Wong DSH,Sandler SI.A theoretically correct mixing rule for cubic EOS[J].AIChE,1992,38:671-380.

同被引文献27

  • 1罗明检,马沛生,夏淑倩.超额Gibbs自由能-状态方程模型计算和预测相平衡的进展[J].石油化工,2005,34(7):694-698. 被引量：6
  • 2常丽萍.煤液化技术研究现状及其发展趋势[J].现代化工,2005,25(10):17-20. 被引量：17
  • 3史士东.煤炭直接液化反应机理和新工艺研究[C].煤炭科学研究总院50周年院庆科技论文集,北京.煤炭工业出版社,2007.501-507.
  • 4朱自强,徐汛.化工热力学[M].北京:化学工业出版社,1992.
  • 5Geprgios M. K, Panayiotis M. V. Aninterpretation of the behavior of EOS-GE models for asymmetric systems [J ]. Chemical Engineering Science. 2000.55:2351 - 2358.
  • 6Huron M J, Vidal J . New Mixing Rules in Simple Equations of State for Representing Vapor-Liquid Equilibria of Srongly Non-Ideal Mixtures [ J ]. Fluid Phase Equilibra, 1979,3:255 - 271.
  • 7Michelsen M L. A Method for Incorporating Excess Gibbs Energy Models in Equations of State [ J ]. Fluid Phase Equilibra, 1990, 60:47 - 58.
  • 8Lermite C, Vidal J. A group contribution Equation of state for polar and non-polar compound [ J ]. Fluid Phase Equilibra, 1992,72 : 111 - 130.
  • 9Michelsen M J. A Method for incorporating Gibbs energy models in equation of state [ J ]. Fluid Phase Equilibra, 1990,60:213 - 216.
  • 10Holderbaum T, Gmehling J. PSRK: A Group Contribution Equation of State Based on UNIFAC [ J ]. Fluid Phase Equilibra, 1991,70 : 251 - 265.

引证文献2

二级引证文献3

重庆三峡学院学报
2006年 第3期

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部