Page 106 - Characterization and Properties of Petroleum Fractions - M.R. Riazi

T1: IML
QC: —/—
P2: —/—
P1: KVU/—
AT029-02
AT029-Manual-v7.cls
AT029-Manual
August 16, 2007
86 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
[63] Pan, H., Firoozabadi, A., and Fotland, P., “Pressure and
Pressure and Related Properties,” Industrial and Engineering
Composition Effect on Wax Precipitation: Experimental Data 16:6 [77] Korsten, H., “Internally Consistent Prediction of Vapor
and Model Results,” Society of Petroleum Engineers Chemistry Research, 2000, Vol. 39, pp. 813–820.
Production and Facilities, Vol. 12, No. 4, 1997, [78] Riazi, M. R. and Daubert, T. E., “Prediction of Molecular Type
pp. 250–258. Analysis of Petroleum Fractions and Coal Liquids,” Industrial
[64] Firoozabadi, A., Thermodynamics of Hydrocarbon Reservoirs, and Engineering Chemistry, Process Design and Development,
McGraw Hill, New York, 1999. Vol. 25, No. 4, 1986, pp. 1009–1015.
[65] Riazi, M. R. and Adwani, H. A., “Some Guidelines for Choosing [79] Won, K. W., Thermodynamics for Solid Solution–Liquid–Vapor
a Characterization Method for Petroleum Fractions in Process Equilibria: Wax Formation from Heavy Hydrocarbon
Simulators,” Chemical Engineering Research and Design, Mixtures,” Fluid Phase Equilibria, Vol. 30, 1986, pp. 265–279.
IchemE, Vol. 83, No. A2, 2005, pp. 160–166. [80] Abbott, M. M., Kaufmann, T. G. and Domash, L., “A Correlation
[66] Vetere, A., “Methods to predict the critical constants of organic for Predicting Liquid Viscosities of Petroleum Fractions,”
compounds,” Fluid Phase Equilibria, Vol. 109, 1995, Canadian Journal of Chemical Engineering, Vol. 49, No. 3, 1971,
pp. 17–27. pp. 379–384.
[67] Riazi, M. R., Daubert, T. E., “Molecular Weight of Heavy [81] Twu, C. H., “Internally Consistent Correlation for Predicting
Fractions from Viscosity,” Oil and Gas Journal, Vol. 58, No. 52, Liquid Viscosities of Petroleum Fractions,” Industrial and
1987, pp. 110–113. Engineering Chemistry, Process Design and Development,
[68] ASTM, Annual Book of Standards, Section Five: Petroleum Vol. 24, 1985, 1287–1293.
Products, Lubricants, and Fossil Fuels (in Five Volumes), [82] Riazi, M. R. and Elkamel, A. “Using Neural Network Models to
ASTM International, West Conshohocken, PA, 2002. Estimate Critical Constants”, Simulators International,
[69] Hirschler, A. E., “Molecular Mass of Viscous Hydrocarbon Oils: International Society for Computer Simulation, Vol. 29, No. 3,
Correlation of Density with Viscosities,” Journal of the Institute 1997, pp. 172–177.
--`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
of Petroleum, Vol. 32, No. 1946, 267, pp. 133–161. [83] Lin, H. M., Kim, H., Guo, T., and Chao, K. C., “Equilibrium
[70] Chorn, L. G. and Mansoori, G. A., C 7+ Characterization, Taylor Vaporization of a Coal Liquid from a Kentucky No. 9 Coal,”
& Francis, New York, 1989. Industrial and Engineering Chemistry, Process Design and
[71] Kesler, M. G., Lee, B. I., and Sandler, S. I., “A Third Parameter Development, Vol. 24, No. 4, 1985, pp. 1049–1055.
for Use in Generalized Thermodynamic Correlations,” [84] Yu, J. M., Wu, R. S., and Batycky, J. P., “A C 7+ Characterization
Industrial and Engineering Chemistry Fundamentals, Vol. 18, Method for Bitumen Mixture Phase Behavior Prediction,”
1979, pp. 49–54. C 7+ Characterization, L. G. Chorn and G. A. Mansoori Eds.,
[72] Lin, H. M. and Chao, K. C., “Correlation of Critical Properties Taylor & Francis, New York, 1989, pp. 169–196.
and Acentric Factor of Hydrocarbons and Derivatives,” [85] Danesh, A., PVT and Phase Behavior of Petroleum Reservoir
American Institute of Chemical Engineers Journal, Vol. 30, Fluids, Elsevier, Amsterdam, 1998.
No. 6, 1984, pp. 981–983. [86] Manafi, H., Mansoori, G. A. and Ghotbi, S., “Phase Behavior
[73] Mobil Oil Company, “Engineering Data Book,” New York, Prediction of Petroleum Fluids with Minimum
1961. Characterization Data,” Journal of Petroleum Science and
[74] Sim, W. J. and Daubert, T. E., “Predcition of Vapor-Liquid Engineering, Vol. 22, 1999, pp. 67–93.
Equilibria of Undefined Mixtures,” Industrial and Engineering [87] Jianzhong, Zh., Biao, Zh., Suoqi, Zh., Renan, W., and
Chemistry, Process Design and Development, Vol. 19, 1980, Guanghua, Y., “Simplified Prediction of Critical Properties of
pp. 386–393. Nonpolar Compounds, Petroleum, and Coal Liquid Fractions,”
[75] Hall, K. R. and Yarborough, L., “New Simple Correlation for Industrial and Engineering Chemistry Research, Vol 37, No. 5,
Predicting Critical Volume,” Chemical Engineering, Vol. 78, 1998, pp. 2059–2060.
No. 25, 1971, p. 76–77. [88] Voulgaris, M., Stamatakis, S., Magoulas, K., and Tassios, D.,
[76] Edmister, W. C., “Applied Hydrocarbon Thermodynamics, Part “Prediction of Physical Properties for nonpolar Compounds,
4: Compressibility Factors and Equations of State,” Petroleum Petroleum, and Coal Liquid Fractions,” Fluid Phase Equilibria,
Refiner, Vol. 37, 1958, pp. 173–179. Vol. 64, 1991, pp. 73–106.

Copyright ASTM International
Provided by IHS Markit under license with ASTM Licensee=International Dealers Demo/2222333001, User=Anggiansah, Erick
No reproduction or networking permitted without license from IHS Not for Resale, 08/26/2021 21:56:35 MDT