Fluid Equations of State

Trebble, M.A. Bishnoi, P.R. Development of a New Four-Parameter Equation of State, Fluid Phase Equilibria, 35, 1-18 (1987). [Pg.402]

Mills, W.B., Dean, J.D., Porcella, D.B., Gherini, S.A., Hudson, R.J.M., Frick, W.E., Rupp, G.L., Bowie, G.L. (1982) Water Quality Assessment A Screening Procedure for Toxic and Conventional Pollutants. Part 1, U.S. EPA, EPA-600/6-82-004a. Mokbel, I., Rauzy, E., Loiseleur, H., Berro, C., Jose, J. (1995) Vapor pressures of 12 alkylcyclohexanes, cyclopentane, butylcyclo-pentane and frara -decahydronaphthalene down to 0.5 Pa. Experimental results, correlation and prediction by an equation of state. Fluid Phase Equil. 108, 103-120. [Pg.401]

Kasehgari, H., Mokbel, I., Viton, C., Jose, J. (1993) Vapor pressure of 11 alkylbenzenes in the range 10 - 280 torn Correlation by equation of state. Fluid Phase Equil. 87, 133-152. [Pg.610]

Chou, G. F., and J. M. Prausnitz Adiabatic flash calculations for continuous or semicontinuous mixtures using an equation of state. Fluid Phase Equilibria, 30,75-82(1986). [Pg.444]

The values in these tables were generated from the NIST REFPROP software (Lemmon, E. W., McLinden, M. O., and Huber, M. L., NIST Standard Reference Database 23 Reference Fluid Thermodynamic and Transport Properties—REFPROP, National Institute of Standards and Technology, Standard Reference Data Program, Gaithersburg, Md., 2002, Version 7.1). The primary source for the thermodynamic properties is Lemmon, E. W, and Ihmels, E. C., Thermodynamic Properties of the Butenes. Part II. Short Fundamental Equations of State, Fluid Those Equilibria 228-2290 173-187, 2005. Validated equations for the viscosity and thermal conductivity are not currently available for this fluid. [Pg.264]

Wisniak, J. Apelblat, A. Segura, H. Prediction of gas-solid equilibrium using equations of state. Fluid Phase Equilibria 1998, 147, 45-64. [Pg.2076]

Soave, G. 20 years of Redlich-Kwong equations of state. Fluid Phase Equilibr. 1993, 82, 345-359. [Pg.2751]

Voutsas, E.C. Kontogeorgis, G.M. Yakoumis, TV. Tassios, D.P. Correlation of liquid-liquid equilibria for alcohol/hydrocarbon mixtures using the CPA equation of state. Fluid Phase Eq. 1997, 132, 61-75. [Pg.2752]

Boukouvalas, C., Spiliotis, N., Coutsikos, P., and Tzouvaras, N., 1994. Prediction of vapor-liquid equilibrium with the LCVM model. A linear combination of the Huron-Vidal and Michelsen mixing rules coupled with the original UNIFAC and the t-mPR equation of state. Fluid Phase Eq., 92 75-106. [Pg.199]

Michelsen, M. L., 1990a. A method for incorporating excess Gibbs energy models in equations of state. Fluid Phase Eq 60 47—58. [Pg.201]

Peneloux, A., Abdoul, W., and Rauzy, E., 1989. Excess functions and equations of state. Fluid... [Pg.202]

Sandoval, R., Wilseck-Vera, G., and Vera, J. H., 1989. Prediction of the ternary vapor-liquid equilibria with the PRSV equation of state. Fluid Phase Eq., 52 119-126. [Pg.203]

Ashour I, Almehaideb R, Fateen SE, Aly G. Representation of solid fluid phase equilibria using cubic equations of state. Fluid Phase Equilibria 2000 167 41-61. [Pg.24]

Zhong, C. and Masuoka, H., Modeling of gas solubilities in polymers with cubic equations of state. Fluid Phase Equilibria, 144, 49, 1998. [Pg.742]

Bertucco, A. and Mio, C., Prediction of vapor-liqnid eqnUibria for polymers with a group contribution equation of state. Fluid Phase Equilibria, 117, 18-25, 1996. [Pg.742]

Tochigi, K., Kurita, S., and Matsumoto, T, Prediction of PVT and VLE in polymer solutions using a cubic-perturbed equation of state, Fluid Phase Equilibria, 158-160, 313, 1999. [Pg.742]

Browarzik, D. and Kowalewski, M., Calculation of the stability and phase equilibrium in the system polystyrene -1- cyclohexane + carbon dioxide based on equations of state. Fluid Phase Equilibria, 163, 43-60, 1999. [Pg.742]

Li, j. D., Vanderbeken, L, Ye, S. Y., Carrier, H. Xans, P. 1997. Prediction of the solubility and gas-liquid equilibria for gas-water and light hydrocarbon-water systems at high temperatures and pressures with a group contribution equation of state. Fluid Phase Equilibria, 131(1/2), 107-118. [Pg.98]

Deiters, U.K. (1985) Calculation of equilibria between fluid and solid phases in binary mixtures at high pressures from equations of state. Fluid Phase Equilibria 20, 275-282. [Pg.66]

Kolafa, J. and Nezbeda, I., 1994. The Lennard-Jones fluid An accurate analytic and theoretically-based equation of state. Fluid Phase Equilib., 100 1. [Pg.245]

Tihic, A., von Sohns, N., Michelsen, M.L., Kontogeorgis, G.M., and Constantinou, L., 2009. Analysis and applications of a group contribution sPC-SAFT equation of state. Fluid Phase Equilib., 281 60. [Pg.246]

Ahlers, J. Gmehling, J. (2001). Development of an universal group contribution equation of state. I. Prediction of liquid densities for pure compounds with a volume translated Peng-Robinson equation of state. Fluid Phase EcjuiUb., Vol.191, pp. 177 -188... [Pg.103]

Kordas, A. Magoulas, K. Stamataki, S. Tassios, D. (1995). Methane hydrocarbon interaction parameters correlation for the Peng-Robinson and the t-mPR equation of state. Fluid Phase Equilib., Vol.112, p>p. 33-44... [Pg.105]

Michelsen, ML. (1990). A modified Huron-Vidal mixing rule for cubic equations of state. Fluid Phase EquUib., Vol.60, p>p. 213-219... [Pg.105]

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