Page 250 - Characterization and Properties of Petroleum Fractions - M.R. Riazi

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230 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
[2] Daubert, T. E., Danner, R. P., Sibul, H. M., and Stebbins, C. C.,
of State for Phase Equilibrium Calculations, 1: Hydrocarbon
Physical and Thermodynamic Properties of Pure Compounds: 17:42 [24] Graboski, M. S. and Daubert, T. E., “A Modified Soave Equation
Data Compilation, DIPPR-AIChE, Taylor & Francis, Bristol, Systems,” Industrial Engineering and Chemistry, Process Design
PA, 1994 (extant) (www.aiche.org/dippr). Updated reference: and Development, Vol. 17, No. 4, 1978, pp. 443–448.
Rowley, R. L., Wilding, W. V., Oscarson, J. L., Zundel, N. A., [25] Twu, C. H., Coon, J. E., and Cunningham, J. R., “A New
Marshall, T. L., Daubert, T. E., and Danner, R. P., DIPPR Data Alpha-Function for a Cubic Equation of State, 1:
Compilation of Pure Compound Properties, Design Institute for Peng-Robinson Equation,” Fluid Phase Equilibria, Vol. 105,
Physical Properties (DIPPR), Taylor & Francis, New York, 2002 No. 1, 1995, pp. 49–59.
(http://dippr.byu.edu). [26] Nasrifar, K. and Moshfeghian, M., “A New Cubic Equation of
[3] AIChE DIPPR R Database, Design Institute for Physical Property State for Simple Fluids, Pure and Mixtures,” Fluid Phase
Data (DIPPR), EPCON International, Houston, TX, 1996 (also Equilibria, Vol. 190, No. 1–2, 2001, pp. 73–88.
see http://dippr.byu.edu). [27] Zudkevitch, D. and Joffe, E., “Correlation and Prediction of
[4] Wagner, W. and Pruss, A., “The IAPWS Formulation for the Vapor–Liquid Equilibria with the Redlich–Kwong Equation
Thermodynamic Properties of Ordinary Water Substance for of State,” American Institute of Chemical Engineers Journal,
General and Scientific Use,” Journal of Physical and Chemical Vol. 16, No. 1, 1970, pp. 112–119.
Reference Data, Vol. 31, No. 2, 2002, pp. 387–535 (also see [28] Joffe, E., Schroeder, G. M., and Zudkevitch, D., “Vapor–Liquid
http://www.iapws.org/). Equilibrium with the Redlich–Kwong Equation of State,”
[5] KISR, Private Communication, Petroleum Research Studies American Institute of Chemical Engineers Journal, Vol. 16,
Center, Kuwait Institute for Scientific Research (KISR), No. 5, 1970, pp. 496–498.
Ahmadi, Kuwait, May 2002. [29] Feyzi, F., Riazi, M. R., Shaban, H. I., and Ghotbi, S.,
[6] Prausnitz, J. M., Lichtenthaler, R. N., and de Azevedo, E.G., “Improving Cubic Equations of State for Heavy Reservoir
Molecular Thermodynamics of Fluid-Phase Equilibria, Fluids and Critical Region,” Chemical Engineering
Prentice-Hall, New Jersey, 1986. Communications, Vol. 167, 1998, pp. 147–166.
[7] Hirschfelder, O. J., Curtiss, C. F., and Bird, R. B., Molecular [30] Abbott, M. M., “Cubic Equations of State: An Interpretive
Theory of Gases and Liquids, Wiley, New York, 1964. Review,” Chapter 3 in Equation of State in Engineering and
[8] Poling, B. E., Prausnitz, J. M., and O’Connell, J. P., Properties of Research, K. C. Chao and R. L. Robinson, Jr., Eds., Advances in
Gases & Liquids, 5th ed., Mc-Graw Hill, New York, 2000. Chemistry Series, American Chemical Society, Washington, DC,
[9] Alberty, R. A. and Silbey, R. J., Physical Chemistry, 2nd ed., Vol. 182, 1979, pp. 47–97.
Wiley, New York, 1999. [31] Martin, J. J., “Cubic Equation of State—Which?,” Industrial
[10] Levine, I. N., Physical Chemistry, 4th ed., McGraw-Hill, New and Engineering Chemistry, Vol. 18, No. 2, 1979, pp. 81–97.
York, 1995. [32] Tsonopoulos, C. and Heidman, J. L., “From Redlich–Kwong to
[11] Redlich, O. and Kwong, J. N. S., “On the Thermodynamics of the Present,” Fluid Phase Equilbria, Vol. 24, 1985, pp. 1–23.
Solutions,” Chemical Review, Vol. 44, 1949, pp. 233–244. [33] Firoozabadi, A., “Reservoir Fluid Phase Behavior and
[12] Soave, G., “Equilibrium Constants from a Modified Volumetric Prediction with Equation of State,” Journal of
Redlich-Kwong Equation of State,” Chemical Engineering Petroleum Technology, Vol. 40, No. 4, 1988, pp. 397–406.
Science, Vol. 27, 1972, pp. 1197–1203. [34] Patel, N. C. and Teja, A. S., “A New Cubic Equation of State
[13] Peng, D. Y. and Robinson, D. B., “A New Two-Constant for Fluids and Fluid Mixtures,” Chemical Engineering Science,
Equation of State,” Industrial and Engineering Chemistry Vol. 77, No. 3, 1982, pp. 463–473.
Fundamentals, Vol. 15, No. 1, 1976, pp. 59–64. [35] Manafi, H., Mansoori, G. A., and Ghotbi, S., “Phase Behavior
[14] Robinson, D. B. and Peng, D. Y., The Characterization of the Prediction of Petroleum Fluids with Minimum
--`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
Heptanes and Heavier Fractions for the GPA Peng-Robinson Characterization Data,” Journal of Petroleum Science and
Programs, Research Report 28, Gas Producers Association Engineering, Vol. 22, 1999, pp. 67–93.
(GPA), Tulsa, 1978. [36] Katz, D. L. and Firoozabadi, A., “Predicting Phase Behavior of
[15] Reid, R. C., Prausnitz, J. M., and Poling, B. E., Properties of Condensate/Crude Oil Systems Using Methane Interaction
Gases & Liquids, 4th ed., McGraw-Hill, New York, 1987. Coefficients,” Journal of Petroleum Technology, Trans., AIME,
[16] Perry, R. H. and Green, D. W., Eds., Chemical Engineers’ Vol. 265, November 1978, pp. 1649–1655.
Handbook, 7th ed., McGraw-Hill, New York, 1997. [37] Chueh, P. L. and Prausnitz, J. M., “Vapor-Liquid Equilibria at
[17] Abramowitz, M. and Stegun, I. A., Handbook of Mathematical High Pressures, Calculation of Partial Molar Volume in
Functions, Dover Publication, New York, 1970. Non-Polar Liquid Mixtures,” American Institute of Chemical
[18] Guo, T. M., Du, L., Pedersen, K. S., and Fredenslund, Aa., Engineers Journal, Vol. 13, No. 6, 1967, pp. 1099–1113.
“Application of the Du-Guo and the SRK Equations of State to [38] Whitson, C. H., Anderson, T. F., and Soreide, I., “C 7+
Predict the Phase Behavior of Chinese Reservoir Fluids,” SPE Characterization of Related Equilibrium Fluids Using the
Reservoir Engineering, Vol. 6, No. 3, 1991, pp. 379–388. Gamma Distribution,” C 7+ Fraction Characterization, L. G.
[19] Whitson, C. H. and Brule, M. R., Phase Behavior, Monograph Chorn and G. A. Mansoori, Eds., Taylor & Francis, New York,
Volume 20, SPE, Richardson, Texas, 2000. 1989, pp. 35–56.
[20] Soreide, I., Improved Phase Behavior Predictions of Petroleum [39] Pedersen, K. S., Thomassen, P., and Fredenslund, Aa., “On the
Reservoir Fluids from a Cubic Euation of State, Dr. Engineering Dangers of “Tuning” Equation of State Parameters,” Chemical
Dissertation, Norwegian Institute of Technology, Trondheim, Engineering Science, Vol. 43, No. 2, pp. 269–278.
Norway, 1989. [40] Whitson, C. H., “Characterizing Hydrocarbon Plus Fractions,”
[21] Danesh, A., PVT and Phase Behavior of Petroleum Reservoir Society of Petroleum Engineers Journal, Trans., AIME, Vol. 275,
Fluids, Elsevier, Amsterdam, 1998. 1983, pp. 683–694.
[22] Peneloux, A., Rauzy, E., and Freze, R., “A Consistent Correction [41] Dymond, J. H. and Smith, E. B., The Virial Coefficients of Pure
for Redlich-Kwong-Soave Volumes,” Fluid Phase Equilibria, Gases and Mixtures, Clarendon Press, Oxford, UK, 1980.
Vol. 8, 1982, pp. 7–23. [42] Tsonopoulos, C., “Empirical Correlation of Second Virial
[23] Jhaveri, B. S. and Youngren, G. K., “Three-Parameter Coefficients,” American Institute of Chemical Engineers Journal,
Modification of the Peng-Robinson Equation of State to Vol. 20, 1974, pp. 263–272.
Improve Volumetric Predictions,” SPE Reservoir Engineering, [43] McGlashan, M. L., Chemical Thermodynamics, Academic Press,
Trans., AIME, Vol. 285, 1998, pp. 1033–1040. New York, 1980.

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