Page 251 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
P. 251

T1: IML
                           QC: IML/FFX
              P2: IML/FFX
  P1: IML/FFX
  AT029-05
                        AT029-Manual-v7.cls
            AT029-Manual
                                           August 16, 2007
                                                                  [65] Spencer, C. F. and Danner, R. P., “Prediction of Bubble Point
            [44] Orbey, H. and Vera, J. H., “Correlation for the Third Virial
                                                                     Pressure of Mixtures,” Journal of Chemical and Engineering
               Coefficient Using T c , P c and ω as Parameters,” American  17:42  5. PVT RELATIONS AND EQUATIONS OF STATE 231
               Institute of Chemical Engineers Journal, Vol. 29, No. 1, 1983,  Data, Vol. 18, No. 2, 1973, pp. 230–234.
               pp. 107–113.                                       [66] Thomson, G. H., Brobst, K. R., and Hankinson, R. W., “An
            [45] Bendict, M., Webb, G. B., and Rubin, L. C., “An Empirical  Improved Correlation for Densities of Compressed Liquids and
               Equation for Thermodynamic Properties of Light        Liquid Mixtures,” American Institute of Chemical Engineers
               Hydrocarbons and Their Mixtures, Methane, Ethane, Propane  Journal, Vol. 28, No. 4, 1982, pp. 671–676.
               and n-Butane,” Journal of Chemical Physics, Vol. 8, 1940,  [67] Tsonopoulos, C., Heidman, J. L., and Hwang, S.-C.,
               pp. 334–345.                                          Thermodynamic and Transport Properties of Coal Liquids, An
            [46] Starling, K. E., Fluid Thermodynamic Properties for Light  Exxon Monograph, Wiley, New York, 1986.
               Petroleum Systems, Gulf Publishing, Houston, TX, 1973.  [68] Garvin, J., “Estimating Compressed Liquid Volumes for
            [47] Prausnitz, J. M., Lichtenthaler, R. N., and de Azevedo, E. G.,  Alcohols and Diols,” Chemical Engineering Progress, 2004,
               Molecular Thermodynamics of Fluid-Phase Equilibria, 3rd ed.,  Vol. 100, No. 3, 2004, pp. 43–45.
               Prentice-Hall, New Jersey, 1999.                   [69] Chueh, P. L. and Prausnitz, J. M., “A Generalized Correlation
            [48] Rao, R. V. G. and Dutta, S. K., “An Equation of State of L-J  for the Compressibilities of Normal Liquids,” American
               Fluids and Evaluation of Some Thermodynamic Properties,”  Institute of Chemical Engineers Journal, Vol. 15, 1969, p. 471.
               Zeitschrift f ¨ ur Physikalische Chemie, Vol. 264, 1983, pp. 771–783.  [70] Riazi, M. R. and Mansoori, G. A., “Simple Equation of State
            [49] Rao, R. V. G. and Gupta, B. D., “Visco-Elastic Properties of  Accurately Predicts Hydrocarbon Densities,” Oil and Gas
               Ionic Liquids,” Acoustics Letter, Vol. 8, No. 9, 1985, pp. 147–149.  Journal, July 12, 1993, pp. 108–111.
            [50] Chapman, W. G., Gubbins, K. E., Jackson, G., and Radosz, M.,  [71] Riazi, M. R. and Roomi, Y., “Use of the Refractive Index in the
               “New Reference Equation of State for Associating Liquids,”  Estimation of Thermophysical Properties of Hydrocarbons and
               Industrial and Engineering Chemistry Research, Vol. 29, 1990,  Their Mixtures,” Industrial and Engineering Chemistry
               pp. 1709–1721.                                        Research, Vol. 40, No. 8, 2001, pp. 1975–1984.
            [51] Li, X.-S. and Englezos, P., “Vapor–Liquid Equilibrium of  [72] Goodwin, R. D., The Thermophysical Properties of Methane from
               Systems Containing Alcohols Using the Statistical Associating  90 to 500 K at Pressures to 700 Bar, National Bureau of
               Fluid Theory Equation of State,” Industrial and Engineering  Standards, NBS Technical Note 653, April 1974.
               Chemistry Research, Vol. 42, 2003, pp. 4953–4961.  [73] Hall, K. R., Ed., TRC Thermodynamic Table—Hydrocarbons,
            [52] Standing, M. B. and Katz, D. L., “Density of Natural Gases,”  Thermodynamic Research Center, Texas A&M University
               AIME Transactions, Vol. 146, 1942, pp. 140–149.       System, 1986.
            [53] Engineering Data Book, Gas Processors (Suppliers) Association,  [74] Goodwin, R. D., Roder, H. M., and Starty, G. C., The
               10th ed., Tulsa, OK, 1987.                            Thermophysical Properties of Ethane from 90 to 600 K at
            [54] Ahmed, T. Reservoir Engineering Handbook, Gulf Publishing,  Pressures to 700 Bar, National Bureau of Standards, NBS
               Houston, TX, 2000.                                    technical note 684, August 1976.
            [55] Hall, K. R. and Yarborough, L., “A New Equation of State for  [75] McCarty, R. D. and Jaconsen, R. T., An Equation of State for
               Z-Factor Calculations,” Oil and Gas Journal, June 18, 1973,  Fluid Ethylene, National Bureau of Standards, NBS Technical
               pp. 82–92.                                            Note 1045, July 1981.
            [56] Pitzer, K. S., Lipmann, D. Z., Curl, R. F., Huggins, C. M., and  [76] Goodwin, R. D. and Hayens, W. M., The Thermophysical
               Petersen, D. E., “The Volumetric and Thermodynamic    Properties of Propane from 85 to 700 K at Pressures to 70 MPa,
               Properties of Fluids, II: Compressibility Factor, Vapor Pressure,  National Bureau of Standards, NBS Monograph 170, April
              --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
               and Entropy of Vaporization,” Journal of American Chemical  1982.
               Society, Vol. 77, 1955, pp. 3433–3440.             [77] Haynes, W. M. and Goodwin, R. D., The Thermophysical
            [57] Pitzer, K. S., Thermodynamics, 3rd ed., MacGraw-Hill, New  Properties of Propane from 85 to 700 K at Pressures to 70 MPa,
               York, 1995.                                           National Bureau of Standards, NBS Monograph 170, April
            [58] Lee, B. I. and Kesler, M. G., “A Generalized Thermodynamic  1982.
               Correlation Based on Three-Parameter Corresponding States,”  [78] Doolittle, A. K., “Specific Volumes of Normal Alkanes,”
               American Institute of Chemical Engineers Journal, Vol. 21, 1975,  Journal of Chemical and Engineering Data, Vol. 9, 1964, pp.
               pp. 510–527.                                          275–279.
            [59] Daubert, T. E. and Danner, R. P., Eds., API Technical Data  [79] Riazi, M. R. and Mansoori, G. A., “Use of the Velocity of Sound
               Book—Petroleum Refining, 6th ed., American Petroleum   in Predicting the PVT Relations,” Fluid Phase Equilibria,
               Institute (API), Washington, DC, 1997.                Vol. 90, 1993, pp. 251–264.
            [60] Elliott, J. R. and Lira, C. T., Introductory Chemical Engineering  [80] Gupta, D. and Eubank, P. T., “Density and Virial Coefficients of
               Thermodynamics, Prentice Hall, New Jersey, 1999       Gaseous Butane from 265 to 450 K Pressures to 3.3 Mpa,”
               (www.phptr.com).                                      Journal of Chemical and Engineering Data, Vol. 42, No. 5,
            [61] Rackett, H. G., “Equation of State for Saturated Liquids,”  Sept.–Oct. 1997, pp. 961–970.
               Journal of Chemical and Engineering Data, Vol. 15, No. 4, 1970,  [81] Konttorp, K., Peters, C. J., and O’Connell, J. P., “Derivative
               pp. 514–517.                                          Properties from Model Equations of State,” Paper presented at
            [62] Spencer, C. F. and Danner, R. P., “Improved Equation for  the Ninth International Conference on Properties and Phase
               Prediction of Saturated Liquid Density,” Journal of Chemical  Equilibria for Product and Process Design (PPEPPD 2001),
               and Engineering Data, Vol. 17, No. 2, 1972, pp. 236–241.  Kurashiki, Japan, May 20–25, 2001.
            [63] Spencer, C. F. and Adler, S. B., “A Critical Review of Equations  [82] Sengers, J. V., Kayser, R. F., Peters, C. J., and White, Jr., H. J.,
               for Predicting Saturated Liquid Density,” Journal of Chemical  Eds., Experimental Thermodynamics, Vol. V: Equations of State
               and Engineering Data, Vol. 23, No. 1, 1978, pp. 82–89.  for Fluids and Fluid Mixtures, IUPAC, Elsevier, Amsterdam,
            [64] Yamada, T. G., “Saturated Liquid Molar Volume: the Rackett  2000.
               Equation,” Journal of Chemical and Engineering Data, Vol. 18,  [83] National Institute of Standards and Technology (NIST),
               No. 2, 1973, pp. 234–236.                             Boulder, CO, 2003, http://webbook.nist.gov/chemistry/fluid/.

















   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
   246   247   248   249   250   251   252   253   254   255   256