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Characterization Data,” Journal of Petroleum Science and
[10] Alberty, R. A. and Silbey, R. J., Physical Chemistry, 2nd ed.,
Wiley, New York, 1999. T1: IML 6. THERMODYNAMIC RELATIONS FOR PROPERTY ESTIMATIONS 295
Engineering, Vol. 22, 1999, pp. 67–93.
[11] Reid, R. C., Prausnitz, J. M., and Poling, B. E., Properties of [33]Pl¨ocker, U., Knapp, H., and Prausnitz, J. M., “Calculation of
Gases and Liquids, 4th ed., Mc-Graw Hill, New York, 1987. High-Pressure Vapor-Liquid Equilibria from a Corresponding
[12] Lenoir, J. M. and Hipkin, H. G., “Measured Enthalpies of Eight States Correlation with Emphasis on Asymmetric Mixtures,”
Hydrocarbon Fractions,” Journal of Chemical and Engineering Industrial and Engineering Chemistry, Process Design and
Data, Vol. 18, No. 2, 1973, pp. 195–202. Development, Vol. 17, No. 13, 1978, pp. 324–332.
[13] AIChE DIPPR® Database, Design Institute for Physical Property [34] Chao, K. C. and Seader, J. D., “A General Correlation of
Data (DIPPR), EPCON International, Houston, TX, 1996 (for Vapor–Liquid Equilibria in Hydrocarbon Mixtures,” American
more updated database from NIST see: http://www.nist.gov/ Institute of Chemical Engineers Journal, Vol. 7, 1961,
srd/fluids.htm and http://webbook.nist.gov/chemistry/fluid/). pp. 598–605.
[14] Wagner, W. and Pruss, A., “The IAPWS Formulation for the [35] Grayson, H. G. and Streed, C. W., “Vapor–Liquid Equlibria for
Thermodynamic Properties of Ordinary Water Substance for High Temperature, High Pressure Hydrogen–Hydrocarbon
General and Scientific Use,” Journal of Physical and Chemical Systems,” Proceedings of the 6th World Petroleum Congress,
Reference Data, Vol. 31, No. 2, 2002, pp. 387–535 (also see: Frankfurt/Main III, Paper 20-PD7, 1963, pp. 233–245.
http://www.iapws.org/). [36] PRO/II, Keyword Manual, Simulation Sciences Inc., Fullerton,
[15] Kesler, M. G. and Lee, B. I., “Improve Prediction of Enthalpy of CA, October 1992.
Fractions,” Hydrocarbon Processing, Vol. 55, 1976, [37] Tsonopoulos, C. and Riazi, M. R., Physical Properties for
pp. 153–158. Engineers, Industrial Course Note for CHE7, OCCD, Kuwait
[16] Tsonopoulos, C., Heidman, J. L., and Hwang, S.-C., University, Kuwait, March 2002.
Thermodynamic and Transport Properties of Coal Liquids,An [38] Li, X.-S. and Englezos, P., “Vapor–Liquid Equilibrium of
Exxon Monograph, Wiley, New York, 1986. Systems Containing Alcohols Using the Statistical Associating
[17] Firoozabadi, A., Thermodynamics of Hydrocarbon Reservoirs, Fluid Theory Equation of State,” Industrial and Engineering
Mc-Graw Hill, New York, 1999. Chemistry Research, Vol. 42, 2003, pp. 4953–4961.
[18] Riazi, M. R. and Daubert, T. E., “Simplify Property Predictions,” [39] Hoffman, A. E., Crump, J. S., and Hocott, C. R., “Equilibrium
Hydrocarbon Processing, Vol. 59, No. 3, 1980, pp.115–116. Constants for a Gas Condensate System,” Transactions of
[19] Denbigh, K., The Principles of Chemical Equilibrium, AIME, Vol. 198, 1953, pp. 1–10.
Cambridge University Press, Cambridge, UK, 1992. [40] Standing, M. B., “A Set of Equations for Computing
[20] Danesh, A., PVT and Phase Behavior of Petroleum Reservoir Equilibrium Ratios of a Crude Oil/Natural Gas System at
Fluids, Elsevier, Amsterdam, 1998. Pressures Below 1000 psia,” Journal of Petroleum Technology,
[21] Prausnitz, J. M., Lichtenthaler, R. N., and de Azevedo, E. G., Vol. 31, 1979 , pp. 1193–1195.
Molecular Thermodynamics of Fluid-Phase Equilibria, [41] Katz, D. L. and Hachmuth, K. H., “Vaporization Equilibrium
Prentice-Hall, New Jersey, 2nd ed., 1986, 3rd ed., 1999. Constants in a Crude-Oil–Natural-Gas System,” Industrial
[22] Sandler, S. I., Chemical and Engineering Thermodynamics, 3rd and Engineering Chemistry Research, Vol. 29, 1937, pp. 1072–
ed., Wiley, New York, 1999. 1077.
[23] Riazi, M. R. and Vera, J. H., “Method to Calculate the Solubility [42] Glaso, O. S., “The Accuracy of PVT Parameters Calculated from
of Light Gases in Petroleum and Coal Liquid Fractions Based Computer Flash Separation at Pressures Less than 1000 psia,”
on their P/N/A Composition,” Industrial and Engineering Journal of Petroleum Technology, Vol. 34, 1982, pp. 1811–1813.
Chemistry Research, Vol. 44, 2005, pp. 186–192. [43] Winnick, J., Chemical Engineering Thermodynamics, Wiley, New
[24] Won, K. W., “Thermodynamics for Solid Solution–Liquid– York, 1997.
Vapor Equilibria: Wax Phase Formation from Heavy [44] Riazi, M. R. and Mansoori, G. A., “Use of the Velocity of Sound
Hydrocarbon Mixtures,” Fluid Phase Equilibria, Vol. 30, in Predicting the PVT Relations,” Fluid Phase Equilibria,
1986, pp. 265–279. Vol. 90, 1993, pp. 251–264.
[25] Pan, H., Firoozabadi, A., and Fotland, P., “Pressure and [45] Riazi, M. R. and Roomi, Y. A., “Use of Velocity of Sound in
Composition Effect on Wax Precipitation: Experimental Data Estimating Thermodynamic Properties of Petroleum
and Model Results,” Society of Petroleum Engineers (SPE) Fractions,” Preprints of Division of Petroleum Chemistry
Production and Facilities, Vol. 12, No. 4, 1993, pp. 250–258. Symposia, American Chemical Society (ACS), Vol. 45, No. 4,
[26] Lira-Galeana, C. A., Firoozabadi, A., and Prausnitz, J. M., 2000, pp. 661–664.
“Thermodynamics of Wax Precipitation in Petroleum [46] Colgate, S. O., Silvarman, A., and Desjupa, C., “Acoustic
Mixtures,” American Institute of Chemical Engineers Journal, Resonance Determination of Sonic Speed and the Critical
--`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
Vol. 42, 1996, pp. 239–248. Point,” Paper presented at the AIChE Spring Meeting, Paper
[27] Pedersen, K. S., Skovborg, P., and Ronningsen, H. P., “Wax No. 29c, New Orleans, 1992.
Precipitation from North Sea Crude Oils, 4: Thermodynamic [47] Colgate, S. O., Silvarman, A., and Desjupa, C., “Sonic Speed
Modeling,” Energy and Fuels, Vol. 5, No. 6, 1991, and Critical Point Measurements in Ethane by the Acoustic
pp. 924–932. Resonance Method,” Fluid Phase Equilibria, Vol. 76, 1992,
[28] Engineering Data Book, 10th ed., Volume II, Sections 17–26, pp. 175–185.
Gas Processors (Suppliers) Association, Tulsa, OK, 1987. [48] Ball, S. J., Goodwin, A. R. H., and Trusler, J. P. M., “Phase
[29] National Institute of Standards and Technology (NIST), Behavior and Physical Properties of Petroleum Reservoir
http://www.nist.gov/srd/fluids.htm and Fluids from Acoustic Measurements,” Journal of Petroleum
http://webbook.nist.gov/chemistry/fluid/ Science and Engineering, Vol. 34, No. 1–4, 2002, pp. 1–11.
[30] Baker, L. E., Pierce, A. C., and Luks, K. D., “Gibbs Energy [49] Mittal Enterprises, New Delhi, India, 2004
Analysis of Phase Equilibria,” Society of Petroleum Engineers (http://www.mittalenterprises.com).
Journal (Trans. AIME), Vol. 273, 1982, pp. 731–742. [50] Alem, A. H. and Mansoori, G. A., “The VIM Theory of
[31] Whitson, C. H. and Brule, M. R., Phase Behavior, Monograph Molecular Thermodynamics,” American Institute of Chemical
Vol. 20, Society of Petroleum Engineers, Richardson, TX, 2000. Engineers Journal, Vol. 30, 1984, pp. 468–480.
[32] Manafi, H., Mansoori, G. A., and Ghotbi, S., “Phase Behavior [51] Walas, S. M., Phase Equilibria in Chemical Engineering,
Prediction of Petroleum Fluids with Minimum Butterworth, London, 1985.
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