Page 401 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
P. 401

P2: IML/FFX
                                        T1: IML
                           QC: IML/FFX
  P1: IML/FFX
                                           June 22, 2007
                        AT029-Manual-v7.cls
                                                        14:25
  AT029-09
            AT029-Manual
                         99.4
                                                                    70.0
                                          ( a )        9. APPLICATIONS: PHASE EQUILIBRIUM CALCULATIONS 381
                                                                                      ( b )
                                                                    65.0
                         99.3
                        Percent of asphaltene precipitated  99.2   Percent of asphaltene precipitated  60.0
                                                                    55.0
                         99.1
                         99.0
                                                                    50.0
                         98.9
                         98.8                                       45.0
                                                                    40.0
                            270 280 290 300 310 320 330 340 350 360    240  250  260  270  280  290  300  310  320
                                           T, K                                       T, K
                                      (a)                                                                            (b)
                              FIG. 9.13—Effect of temperature on asphaltene precipitation. (a) Propane diluent; (b)
                            n-heptane diluent. Taken with permission from Ref. [39].
            c. In calculation of f /f i S  parameters T Mi ,  H , and  C Pi  Pedersen et al. [42], based on their data for North Sea oils,
                              L
                                                    f
                                                    i
                              i
              must be calculated for each component i.            showed that both Won and Hansen procedures significantly
                                           f
            d. Calculate T Mi from Eq. (6.156),  H from Eq. (6.157), and  overestimate both the amount of wax precipitation and CPT.
                                           i
               C Pi from Eq. (6.161).                             For this reason, they suggested a number of adjustable pa-
                           L
                                 S
            e. Calculate both γ and γ from Eq. (6.154). In calculation of  rameters to be used for calculation of various parameters.
                           i
                                 i
                         S
                                          S
                                                L
               S
              γ , calculate δ from Eq. (6.155). V and V can be obtained  Chung [44] has used the following empirical set of correla-
               i
                                          i
                         i
                                                i
              from Table 7.1.                                     tions for calculation of properties of C 7+ fractions for the wax
                    L
                       S
                          L
            f. Once f /f , γ , and γ i S  have been determined, calculate  formation prediction:
                    i
                      i
                         i
              K SL  from Eq. (6.209).
               i                                                            f         0.55
                                                                          H = 0.9T Mi M i
                                                                           i
                                                                           L
            This is a typical solid–solution model for calculation of wax  V = 3.8M 0.786
                                                                           i
                                                                                   i
            formation without the use of any adjustable parameter. All pa-  (9.22)  L                        2
            rameters can be calculated from the molecular weight of com-  δ = 6.743 + 0.938 (ln M i) − 0.0395 (ln M i)
                                                                           i
            ponents or pseudocomponents as described in Sections 6.6.6.        −13.039 (ln M i) −1
            Using PNA composition for calculation of properties of C 7+
                                                                                                        f
            pseudocomponents through Eqs. (6.149), (6.156), and (6.157)  where T Mi is the melting point in kelvin,  H is the molar
                                                                                                        i
                                                                                         L
            improves model predictions.                           heat of fusion in cal/mol, V is the molar liquid volume in
                                                                                         i
                                    FIG. 9.14—Effect of pressure on asphaltene precipitation. Taken with
                                  permission from Ref. [40].














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