高等学校化学学报 ›› 2009, Vol. 30 ›› Issue (8): 1631.

• 研究论文 • 上一篇    下一篇

超临界CO2与叔丁醇二元系统高压相平衡研究

王琳1,2, 李入林3, 孙林涛1, 陈开勋1   

  1. 1. 西北大学化工学院, 西安 710069;
    2. 南阳师范学院化学与制药工程学院, 南阳 473061;
    3. 南阳理工学院生化系, 南阳 473004
  • 收稿日期:2008-11-03 出版日期:2009-08-10 发布日期:2009-08-10
  • 通讯作者: 陈开勋, 男, 教授, 主要从事超临界流体技术及相关研究. E-mail: kxchen@nwu.edu.cn

Studies on Phase Equilibrium of Tertbutanol in Supercritical CO2

WANG Lin1,2, LI Ru-Lin3 , SUN Lin-Tao1 , CHEN Kai-Xun1*   

  1. 1. Chemical Engineering College, Northwest University, Xi′an 710069, China;
    2. Chemistry and Pharmaceutical Engineering College, Nanyang Normal University, Nanyang 473061, China;
    3. Biochemical Engineering College, Nanyang Science Institute, Nanyang 473004, China
  • Received:2008-11-03 Online:2009-08-10 Published:2009-08-10
  • Contact: CHEN Kai-Xun. E-mail: kxchen@nwu.edu.cn

摘要:

采用固定体积可视观察法测量装置测定了CO2与叔丁醇在323.2~353.2 K温度范围内于不同压力下的平衡数据, 并运用Peng-Robinson状态方程(PR)和Van der Waals-2混合规则建立了相平衡模型, 通过非线性最小二乘法优化计算得到了不同温度下的模型参数. 并得到了模型参数与温度的表达式, 分别为k12=-199.2066+1.8136T-0.00548T2+5.50×10-6T3; n12=-384.5626+3.4960T-0.01056T2+1.06×10-5T3.获得了此体系在不同组成下的临界压力、临界温度、临界摩尔体积、临界压缩因子和临界密度等临界性质. 研究结果表明, CO2与叔丁醇二元体系的临界温度、临界压力和临界压缩因子均随着临界CO2组成的增加而降低.

关键词: 超临界二氧化碳; 叔丁醇; 相平衡模型; 临界性质

Abstract:

Vapor-liquid phase equilibrium data of tertbutanol in the SC-CO2 from 323.2 K to 353.2 K were determined by constant-volume visual method. The phase equilibrium model was established by Peng-Robinson equation of state and Vander Waals-2 mixed regulation. Model parameters were obtained by nonlinear least square method optimization calculation. Furthermore, the correlation equations of model parameters vs. temperature were obtained: k12=-199.2066+1.8136T-0.00548T2+5.50×10-6T3, n12=-384.5626+3.4960T-0.01056T2+1.06×10-5T3. Critical properties of critical pressure, critical temperature, critical molar volume and critical density were deduced. The results showed that critical temperature, critical pressure and critical compressibility factor of CO2-tertbutanol system would decrease with the increasement of critical CO2 content.

Key words: Supercritical carbon dioxide; Tertbutanol; Phase equilibrium model; Critical property

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