Page 194 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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         174 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
                                                                      10
                 4
                                                                       8
                 3
                PDF, F(T b*)  2                                      PDF, F(SG * )  6
                 1                                                     4
                                                                       2
                 0
                   0     0.2    0.4   0.6    0.8    1                  0
                                   T *                                   0      0.1      0.2      0.3     0.4
                                    b
                                                                                         SG *
               0.012
                                                                      14
                                                                      12
               0.009                                                  10
             PDF, F(T b )  0.006                                    PDF, F(SG)  8






               0.003                                                  6
                                                                      4
                                                                      2
                  0
                   300    400    500   600    700    800              0
                                                                       0.7         0.8         0.9         1
                             Boiling Point, T  , K                                Specific Gravity, SG
                                         b
             FIG. 4.14—Prediction of PDF for boiling point by       FIG. 4.15—Prediction of PDF for specific gravity by
           Eqs. (4.66) and (4.70) for the system of Example 4.7.
                                                                   Eqs. (4.66) and (4.70) for the system of Example 4.7.
         to 3. If these fix values are used errors for prediction of  From Eq. (4.16) and in terms P , the PDF is given as
                                                                                         ∗
         distribution of M, T b , and SG through Eq. (4.56) increases
         slightly as shown in Table 4.13.                     (4.65)              F(P ) =  dx c
                                                                                     ∗
                                                                                         dP  ∗
                                                                       ∗
          In Example 4.7, method of determination of three coef-  where F(P ) is the PDF in terms of dimensionless parameter
                                                                ∗
         ficients of Eq. (4.56) was demonstrated. As shown in this  P which can be determined by differentiation of Eq. (4.64)
                                                                             ∗
         example fixed values of B (B M = 1, B T = 1.5, B SG = 3, B I = 3)  with respect to P according to the above equation:
         may be used for certain mixtures especially for gas conden-              B 2  ∗B−1     B  ∗B
                                                                              ∗
         sate systems and light oils, which reduce the distribution  (4.66)  F(P ) =  A  P  exp −  A  P
         model into a two-parameter correlation. It has been observed
            --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
         that even for most oil samples the fixed values of B T = 1.5 and  Equation (4.66) is in fact the probability density function for
         B SG = B I = 3 are also valid. Further evaluation of Eq. (4.56)  the generalized distribution model of Eq. (4.56) in terms of
                                                                         ∗
         as a three-parameter or a two-parameter correlation and a  parameter P . In a hydrocarbon plus fraction, parameter P ∗
         comparison with the gamma distribution model are shown  varies from 0 to ∞. Application of Eq. (4.17) in terms of P ∗
         in Section 4.5.4.5.                                  gives:
                                                                                 ∞

         4.5.4.2 Probability Density Function for the Proposed  (4.67)             F(P )dP = 1
                                                                                      ∗
                                                                                          ∗
         Generalized Distribution Model
                                                                                 0
         The distribution model expressed by Eq. (4.56) can be trans-  and x c at P can be determined from Eq. (4.18) in terms
                                                                         ∗
         formed into a probability density function by use of Eq. (4.16).  of P :
                                                                  ∗
         Equation (4.56) can be rearranged as
                                                                                      ∗
                                                                                     P
                                     B                        (4.68)            x c =  F(P )dP  ∗
                                                                                          ∗

        (4.64)          1 − x c = exp −  P ∗B
                                     A                                               0




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