节点文献

煤炭直接液化体系高温高压气液相平衡研究进展及模型选择

Development and model selection of vapor-liquid equilibria at high temperatures and high pressures for direct coal liquefaction system

  • 推荐 CAJ下载
  • PDF下载
  • 不支持迅雷等下载工具,请取消加速工具后下载。

【作者】 毛学锋胡发亭史士东艾军

【Author】 MAO Xue-feng,HU Fa-ting,SHI Shi-dong,AI Jun(Beijing Research Institute of Coal Chemistry, China Coal Research Institute, Beijing 100013, China)

【机构】 煤炭科学研究总院北京煤化工研究分院

【摘要】 笔者从气液相平衡基础理论展开并综述了高温高压相平衡计算研究进展,介绍了状态方程法、混合模型法、超额Gibbs自由能—状态方程模型法,并重点介绍了超额Gibbs自由能—状态方程模型法的思路及应用特点。针对煤炭直接液化物系高温、高压、强不对称、强极性、完全非理想体系等特点,与结合传统混合规则的状态方程法及混合模型法相比较,采用超额Gibbs自由能—状态方程模型法能够在更大范围内准确计算和预测煤液化气液相平衡。

【Abstract】 The article firstly spreads out exposition of the basic theory of vapor-liquid equilibria and the development of phase equilibrium calculation at high temperatures and high pressures was reviewed. Several models such as equation of state model, mixing model,Gibbs free energy-equation of state model were introduced. The research thought and application characteristics of Gibbs free energy-equation of state model were emphatically introduced. In accordance with the characteristic of high temperature,high pressure,strong asymmetry,strong polar,completely non-ideal system for direct coal liquefaction, the Gibbs free energy-equation of state model gave more precise result than equation of state model with conventional mixing rule and mixing model.

【基金】 国家重点基础研究发展计划973项目(2004CB217604)
  • 【文献出处】 洁净煤技术 ,Clean Coal Technology , 编辑部邮箱 ,2009年05期
  • 【分类号】TQ529.1
  • 【被引频次】3
  • 【下载频次】138
节点文献中: 

本文链接的文献网络图示:

本文的引文网络