Abstract
We predict the viscosity of petroleum fractions using extended corresponding states. Our model builds upon the TRAPP procedure, which is the most advanced approach to predict transport properties of straight-chain nonpolar hydrocarbons and their mixtures. We perform comparisons with experimental viscosity data for pure hydrocarbons, treating them as nonstandard components; we find deviations of 10–15%. We also extend the model to predict the transport properties of petroleum fractions and compare with an experimental database of more than 80 crude oils, including highly aromatic petroleum fractions. The model predicts the viscosity of the crude oil fractions within experimental uncertainty.
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References
K. C. Mo and K. E. Gubbins,Mol. Phys. 31:825 (1976).
H. J. M. Hanley,Cryogenics 16:643 (1976)
J. F. Ely and H. J. M. Hanley,Ind. Eng. Chem. Fundam. 20:323 (1981).
J. F. Ely and H. J. M. Hanley,Ind. Eng. Chem. Fundam. 22:90 (1983).
B. A. Younglove and J. F. Ely,J. Phys. Chem. Ref. Data 16:577 (1987).
J. W. Leach, P. S. Chappelear, and T. W. Leland,AIChE J. 14:568 (1968).
J. F. Ely,Adv. Cryogen. Eng. 35:1511 (1981).
M. L. Huber and J. F. Ely,Int. J. Refrig. 17:18 (1994).
M. Baltatu,Ind. Eng. Chem. Process Des. Der. 21:192 (1982).
M. E. Baltatu, J. F. Ely, H. J. M. Hanley, M. S. Graboski, R. A. Perkins, and E. D. Sloan,Ind. Eng. Process Des. Dev. 24:325 (1985)
J. B. Maxwell,Data Book on Hydrocarbons (Van Nostrad, Princeton, NJ, 1950).
M. R. Riazi, Ph.D. thesis (Department of Chemical Engineering, Pennsylvania State University, University Park, 1979).
B. I. Lee and M. G. Kesler,Hydrocarbon Process. 55:153 (1976).
C. H. Twu,Fluid Phase Equil. 16:137 (1984).
API Technical Data Book, 4th ed. (1988).
B. I. Lee and M. G. Kesler,Hydrocarbon Process. 59:163 (1980). Erratum,Hydrocarbon Process. 59:91 (1980).
J. B. Maxwell and L. S. Bonnell,Ind. Eng. Chem. 49:1187 (1957).
R. W. Hankinson and G. H. Thomson,AIChE J. 25:653 (1979).
M. E. Baltatu, R. W. Hankinson, and G. H. Thomson,Proc. 66th GPA Conv. (1987).
M. L. Huber and H. J. M. Hanley, IUPAC VolumeTransport Properties of Fluids, J. H. Dymond, J. Millat, and C. A. Nieto de Castro, eds. (in press), Chap. 11.
J. F. Ely and M. L. Huber,NIST Standard Reference Database 4, Computer Program SUPERTRAPP, NIST Thermophysical Properties of Hydrocarbon Mixtures, Version 1.04 (1990). Also, see M. L. Huber and J. F. Ely, Fluid Phase Equil. 80:239 (1992).
API Crude Characterization Study, NIPER B08770-3, Nov. (1993).
W. F. Bland and R. L. Davidson,Petroleum Processing Handbook (McGraw-Hill, New York, 1967).
S. A. Beg, M. B. Amin, and I. Hussain,Chem. Eng. J. 38:123 (1988).
M. Kanti,J. Phys. Chem. 93:3860 (1989)
A. E. Becker and H. G. M. Fischer,SAE J. 35:376 (1934).
S. P. Cauley and E. B. Delgass,Oil Gas J. 45:166 (1946).
W. C. Edminster and D. H. Pollock,Chem. Eng. Progr. 44:905 (1948).
R. C. Mithoff, G. R. MacPherson, and F. Sipos,Oil Gas J. 40:81 (1941).
K. M. Watson, E. F. Nelson, and G. B. Murphy,Ind. Eng. Chem. 27:1460 (1935).
M. B. Amin and R. N. Maddox,Hydrocarbon Process. 12:131 (1981).
N. V. K. Dutt,Cherry. Eng. J. 45:83 (1990).
S. I. Sandler and H. Orbey,Can. J. Chem. Eng. 71:437 (1993).
C. H. Twu,I & EC Process Design Der. 24:1287 (1985.
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Baltatu, M.E., Chong, R.A. & Huber, M.L. Viscosity of defined and undefined hydrocarbon liquids calculated using an extended corresponding-states model. Int J Thermophys 17, 213–221 (1996). https://doi.org/10.1007/BF01448223
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DOI: https://doi.org/10.1007/BF01448223