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Received August 20, 2007
Accepted April 13, 2008
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Phase equilibria behavior of carbon dioxide-n-hexane-naphthalene ternary system
Department of Chemical Engineering, King Saud University, Riyadh 11421, Saudi Arabia 1Chemical Engineering Department, Kuwait University, Safat 13060, Kuwait
alnashef@ksu.edu.sa
Korean Journal of Chemical Engineering, November 2008, 25(6), 1495-1498(4), 10.1007/s11814-008-0246-4
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Abstract
The ternary system CO2-n-hexane-naphthalene was studied to determine the bubble point pressure at three different temperatures (40, 60 and 80 ℃) 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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AlSahhaf TA, AI-Ameeri RS, AlNashef IM, Hamam SEM, Fluid Phase Equilibria, 55, 231 (1990)
Barrick MW, Anderson JM, Robinson Jr. RL, J. Chem. Eng. Data, 32, 372 (1987)
Li YH, Dillard KH, Robinson Jr. RL, J. Chem. Eng. Data, 26, 55 (1981)
Kaminishi GI, Yokoyama C, Takahashi S, Fluid Phase Equilibria, 34, 83 (1987)
Morris OW, Donohue MD, J. of Chem. Eng. Data, 30, 259 (1985)
Peng DY, Robinson DB, Ind. Eng Chem. Fundam., 15, 59 (1976)
Reid RC, Prausnitz JM, Poling EB, The properties of gases and liquids, 4th ed., McGraw-Hill, USA (1988)
Vergaftik NB, Tables of the thermophysical properties of liquids and gases, 2nd edition, Wiley, USA (1975)
Kulkarni AA, Luks KD, Kohn JP, J. of Chem. Eng. Data, 19, 349 (1974)
Yang HW, Luks KD, Kohn JP, J. of Chem. Eng. Data, 21, 330 (1976)
Nieuwoudt I, du Rand M, J. Supercrit. Fluids, 22(3), 185 (2002)
