Page 415 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
P. 415

P2: IML/FFX
  P1: IML/FFX
                                                        14:25
            AT029-Manual
  AT029-09
                                           June 22, 2007
                        AT029-Manual-v7.cls
                  temperature must be near the temperature calculated
                                                                  [16] Firoozabadi, A., Thermodynamics of Hydrocarbon Reservoirs,
                                                                     McGraw-Hill, New York, 1999.
                  in part b.  QC: IML/FFX  T1: IML     9. APPLICATIONS: PHASE EQUILIBRIUM CALCULATIONS 395
            9.11. For the reservoir fluid of Problem 9.10 calculate the  [17] Pan, H., Firoozabadi, A., and Fotland, P., “Pressure and
                amount of wax precipitated (in mol%) at 280, 300, and  Composition Effect on Wax Precipitation: Experimental
                320 K and 410 bar. Also estimate WAT at 410 bar using  Data and Model Results,” Society of Petroleum Engineers
                solid solution model.                                (SPE) Production and Facilities, Vol. 12, No. 4, 1997,
                                                                     pp. 250–258.
            9.12. Calculate the CPT for crude oil 6 in Table 9.10 using  [18] Dubey, S. T. and Waxman, M. H., “Asphaltene Adsorption and
                multisolid-phase model. Also calculate the amount of  Desorption from Mineral Surface,” SPE, Paper No. 18462,
                wax precipitation in wt% at 240 K.                   1989, pp. 51–62.
            9.13. A natural gas has the composition of 70 mol% methane,  [19] Yen, T. F. and Chilingarian, G. V., Asphaltenes and Asphalts,
                15 mol% ethane, 7 mol% propane, 5 mol% n-butane, and  Development in Petroleum Sciences, 40A, Elsevier Science,
                3 mol% H 2 S. What is the hydrate formation temperature  Amsterdam, 1994.
                (HFT) for this gas at pressure of 15 bars? What methanol  [20] Pan, H. and Firoozabadi, A., “Thermodynamic
                solution (in terms of wt%) is needed to reduce HFT of  Micellization Model for Asphaltene Aggregation and
                the gas to 0 C?                                      Precipitation in Petroleum Fluids,” Society of Petroleum
                          ◦
            9.14. A gas mixture of 75 mol% C 1 , 10 mol% C 2 , 10 mol%  Engineers (SPE) Production and Facilities, Vol. 13, May 1998,
                                                                     pp. 118–127.
                C 3 , and 5 mol% n-C 4 exists at 690 bars. Calculate hy-  [21] ASTM, Annual Book of Standards, Section Five: Petroleum
                drate formation temperature and the concentration of  Products, Lubricants, and Fossil Fuels (in 5 Vols.), ASTM
                methanol solution required to reduce it to 10 C.     International, West Conshohocken, PA, 2002.
                                                      ◦
                                                                  [22] Standard Methods for Analysis and Testing of Petroleum and
                                                                     Related Products and British Standard 2000 Parts, IP 1–324
                                                                     Vol. 1, IP 325–448, Vol. 2, The Institute of Petroleum, London,
            REFERENCES                                               1999.
                                                                  [23] Goual, L. and Firoozabadi, A., “Measuring Asphaltenes and
             [1] Whitson, C. H. and Brule, M. R., Phase Behavior, Monograph  Resins, and Dipole Moment in Petroleum Fluids,” American
               Vol. 20, Society of Petroleum Engineers, Richardson, TX,  Institute of Chemical Engineers Journal, Vol. 48, No. 11, 2002,
               2000.                                                 pp. 2646–2662.
             [2] Ahmed, T., Hydrocarbon Phase Behavior, Gulf Publishing,  [24] Kim, S. T., Boudth-Hir, M. E., and Mansoori, G. A., “The Role
               Houston, TX, 1989.                                    of Asphaltene in Wettability Reversal,” Paper No. 20700, Paper
             [3] Danesh, A., PVT and Phase Behavior of Petroleum Reservoir  presented at the 65th Annual Technical Conference and
               Fluids, Elsevier, Amsterdam, 1998.                    Exhibition of Society of Petroleum Engineers, New Orleans, LA,
             [4] Elliott, J. R. and Lira, C. T., Introductory Chemical Engineering  September 23–26, 1990.
               Thermodynamics, Prentice Hall, New Jersey, 1999    [25] Kawanaka, S., Park, S. J., and Mansoori, G. A., “The Role of
               (www.phptr.com).                                      Asphaltene Deposition in EOR Gas Flooding: A Predictive
             [5] Michelsen, M. L., “The Isothermal Flash Problem. Part I:  Technique,” Paper No. 17376, Paper presented at the SPE/DOE
               Stability,” Fluid Phase Equilibria, Vol. 9, No. 1, 1982, pp. 1–19.  Enhanced Oil Recovery Symposium, Tulsa, OK, April 17–20,
             [6] Michelsen, M. L., “The Isothermal Flash Problem. Part II:  1988.
               Phase Split Calculation,” Fluid Phase Equilibria, Vol. 9, No. 1,  [26] Zou, R. and Liu, L., “The Role of Asphaltene in Petroleum
               1982, pp. 21–40.                                      Cracking and Refining,” in Asphlatenes and Asphalts, I:
             [7] Riazi, M. R., Aladwani, H. A., and Bishara, A.,     Developments in Petroleum Science, Vol. 40, Yen, T. F. and
               “Characterization of Reservoir Fluids and Crude Oils: Options  Chilingarian, G. V., Eds., Elsevier, Amsterdam, 1994, Ch. 14,
               and Restrictions,” Journal of Petroleum Science and   pp. 339–363.
               Engineering, Vol. 44, No. 2–4, 2004, pp. 195–207.  [27] Escobedo, J. and Mansoori, G. A., “Asphaltene and Other
             [8] Riazi, M. R., “Improved Phase Behavior Calculations of  Heavy Organic Particle Deposition During Transfer and
               Reservoir Fluids Using a Distribution Model,” International  Production Operation,” Paper No. 30672, Paper presented at
               Journal of Science and Technology (Scientia), Vol. 10, No. 2,  the SPE Annual Technical Conference and Exhibition, Dallas,
               2003, pp. 341–345.                                    TX, October 22–25, 1995.
             [9] “EOR V90.2 Simulator from DB Robinson for Phase Behavior  [28] Riazi, M. R. and Merrill, R. C., Eds., “Petroleum Exploration
               Calculations,” D. B. Robinson and Associates, Edmonton,  and Production Research in the Middle East,” Journal of
               Alberta, Canada, 1995 (www.dbra.com).                 Petroleum Science and Engineering, Vol. 42, Nos. 2–4, April
            [10] Ahmed, T., Reservoir Engineering Handbook, Gulf Publishing,  2004, pp. 73–272 (http://www.elsevier.com/locate/petrol/).
               Houston, TX, 2000.                                 [29] Mansoori, G. A., “Modeling of Asphaltene and Other Heavy
            [11] Li, C. C., “Critical Temperature Estimation for Simple  Organic Depositions,” Journal of Petroleum Science and
               Mixtures,” Canadian Journal of Chemical Engineering, Vol. 49,  Engineering, Vol. 17, 1997, pp. 101–111.
               No. 5, 1971, pp. 709–710.                          [30] Kawanaka, S., Park, S. J., and Mansoori, G. A., “Organic
            [12] Daubert, T. E. and Danner, R. P., Eds., API Technical Data  Deposition from Reservoir Fluids: A Thermodynamic
               Book—Petroleum Refining, 6th ed., American Petroleum   Predictive Technique,” SPE Reservoir Engineering, Vol. 6, May
               Institute (API), Washington, DC, 1997.                1991, pp. 185–192.
            [13] Kreglewski, A. and Kay, W. B., “The Critical Constants of  [31] Janradhan, A. S. and Mansoori, G. A., “Fractal Nature of
               Conformal Mixtures,” Journal of Physical Chemistry, Vol. 73,  Asphaltene Aggregation,” Journal of Petroleum Science and
               No. 10, 1969, pp. 3359–3366.                          Engineering, Vol. 9, 1993, pp. 17–27.
            [14] Pedersen, K. S., Fredenslund, Aa., and Thomassen, P., Properties  [32] Mousavi-Dehghani, S. A., Riazi, M. R., Vafaie-Sefti, M., and
               of Oils and Natural Gases, Gulf Publishing, Houston, TX, 1989.  Mansoori, G. A., “An Analysis of Methods for Determination of
            [15] Speight, J. G., The Chemistry and Technology of Petroleum, 3rd  Onsets of Asphaltene Phase Separations,” Journal of Petroleum
               ed., Marcel Dekker, New York, 1999.                   Science and Engineering, Vol. 42, 2004, pp. 145–156.













                        --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
   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
   410   411   412   413   414   415   416   417   418   419   420