Phase equilibria behavior of carbon dioxide-n-hexane-naphthalene ternary system

被引：0
作者：
Inas Muen AlNashef
Rasheed S. Al-Ameeri
Taher A. Al Sahhaf
Salah E. M. Hamam
机构：
[1] Kuwait University,Department
[2] King Saud University,Department of Chemical Engineering
来源：
Korean Journal of Chemical Engineering | 2008年 / 25卷
关键词：
Phase Equilibria; Ternary System; Carbon Dioxide; Hydrocarbons; Peng-Robinson Eqation of State;
D O I：
暂无
中图分类号：
学科分类号：
摘要：
The ternary system CO2-n-hexane-naphthalene was studied to determine the bubble point pressure at three different temperatures (40, 60 and 80 °C) and a fixed n-hexane to naphthalene mole ratio of 9: 1. The experimental data obtained were predicted by using the Peng-Robinson equation of state with two interaction parameters. The experimental and calculated bubble point pressures were generally in good agreement at the three temperatures and over the composition range investigated.
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页码：1495 / 1498
页数：3
相关论文
共 32 条
  • [1] Brunner G.(1995)undefined Fluid Phase Equilibria 106 213-undefined
  • [2] Dohrn R.(2002)undefined Fluid Phase Equilibria 202 153-undefined
  • [3] Christov M.(1987)undefined Fluid Phase Equilibria 34 83-undefined
  • [4] Dohrn R.(1990)undefined Fluid Phase Equilibria 55 231-undefined
  • [5] AlSahhaf T. A.(1987)undefined J. Chem. Eng. Data 32 372-undefined
  • [6] AI-Ameeri R. S.(1981)undefined J. Chem. Eng. Data 26 55-undefined
  • [7] Hamam S. E. M.(1987)undefined Fluid Phase Equilibria 34 83-undefined
  • [8] AlSahhaf T. A.(1985)undefined J. of Chem. Eng. Data 30 259-undefined
  • [9] AI-Ameeri R. S.(1976)undefined Ind. Eng Chem. Fundam. 15 59-undefined
  • [10] AlNashef I. M.(1974)undefined J. of Chem. Eng. Data 19 349-undefined
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