Page 88 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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         68 CHARACTERIZATION AND PROPERTIES OF PETROLEUM FRACTIONS
         of −0.0004 in Eq. (2.118)) as a function of n 20 rather than
         a constant. Another approach to estimate refractive index  determined the atomic HC ratio can be calculated from their
                                                              definitions as described in Section 2.1.18:
         at temperatures other than 20 C is to assume that specific
                                  ◦
         refraction is constant for a given hydrocarbon:      (2.122)   HC (atomic ratio) =  11.9147
                                                                                         CH(weight ratio)
                                  I T  I 20
        (2.119)  Specific refraction =  =  = constant
                                  d T  d 20                   Example 2.9—Estimate the values of CH (weight) and HC
         where I 20 is the refractive index parameter at 20 C and I T is its  (atomic) ratios for n-tetradecylbenzene (C 20 H 34 ) from Eqs.
                                               ◦
         value at temperature T. Similarly d T is density at temperature  (2.120) and (2.121) and compare with the actual value. Also
         T. In fact the value of specific refraction is the same at all tem-  draw a graph of CH values from C 6 to C 50 for the three homol-
         peratures [38]. If I 20 , d 20 , and d T are known, then I T can be esti-  ogous hydrocarbon groups from paraffins, naphthenes, and
         mated from the above equation. Value of n T can be calculated  aromatics based on Eq. (2.121) and actual values.
         from I T and Eq. (2.114). Equation (2.119) has the same accu-
         racy as Eq. (2.118), but at the temperatures far from the refer-  Solution—The actual values of CH weight and HC
         ence temperature of 20 C accuracy of both methods decrease.  atomic ratios are calculated from the chemical formula
                           ◦
         Because of simplicity, Eq. (2.118) is recommended for calcu-  and Eq. (2.122) as CH = (20 × 12.011)/(34 × 1.008) = 7.01,
         lation of refractive index at different temperatures. It is obvi-  HC (atomic) = 34/20 = 1.7. From Table 2.1, for n-tetradecyl-
         ous that the reference temperature in both Eqs. (2.118) and  benzene (C 20 H 34 ), T b = 627 K and SG = 0.8587. Substitut-
         (2.119) can be changed to any desired temperature in which  ing these values into Eq. (2.120) gives CH = 7.000, and from
         refractive index is available. Refractive index is also related to  Eq. (2.122) atomic HC ratio = 1.702. The error from
         another property called dielectric constant, ε, which for non-  Eq. (2.134) is %D = 0.12%. Equation (2.121) gives CH =
                                              2
         polar compounds at any temperature is ε = n . For example,  6.998, which is nearly the same as the value obtained from --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
         at temperature of 20 C, a paraffinic oil has dielectric constant  Eq. (2.120) with the same error. Similarly CH values are cal-
                         ◦
                                         2
         of 2.195 and refractive index of 1.481 (n = 2.193). Dielectric  culated by Eq. (2.121) for hydrocarbons ranging from C 6 to
         constants of petroleum products may be used to indicate the  C 50 in three homologous hydrocarbon groups and are shown
         presence of various constituents such as asphaltenes, resins,  with actual values in Fig. 2.10.
         etc. [11]. However, for more complex and polar molecules
         such as multiring aromatics, this simple relation between ε  2.6.4 Prediction of Freezing/Melting Point
             2
         and n is not valid and they are related through dipole mo-
         ment. Further discussion on the methods of estimation of  For pure compounds, the normal freezing point is the same
         refractive index is given by Riazi and Roomi [37].   as the melting point, T M . Melting point is mainly a param-
                                                              eter that is needed for predicting solid–liquid phase behav-
                                                              ior, especially for the waxy oils as shown in Chapter 9. All
         2.6.3 Prediction of CH Weight Ratio
                                                              attempts to develop a generalized correlation for T M in the
         Carbon-to-hydrogen weight ratio as defined in Section 2.1.18  form of Eq. (2.38) have failed. However, Eq. (2.42) developed
         is indicative of the quality and type of hydrocarbons present  by Riazi and Sahhaf for various homologous hydrocarbon
         in a fuel. As will be shown in Chapter 3 from the knowledge  groups can be used to estimate melting or freezing point of
         of CH value, composition of petroleum fractions may be es-  pure hydrocarbons from C 7 to C 40 with good accuracy (error
         timated. CH value is also related to carbon residues as it is  of 1–1.5%) for practical calculations [31]. Using this equation
         discussed in the next chapter. For hydrocarbons with molec-  with appropriate constants in Table 2.6 gives the following
         ular weight in the range of 70–300, the relations to estimate  equations for predicting the freezing point of n-alkanes (P),
         CH values are given through Eq. (2.40) and Table 2.5. In terms  n-alkycyclopentanes (N), and n-alkybenzenes (A) from molec-
         of T b and SG the relation is also given by Eq. (2.120) which  ular weight.
         is also recommended for use in prediction of composition of                                 0.47
         petroleum fractions [78].                            (2.123)  T MP = 397 − exp(6.5096 − 0.14187M  )
                                        −2
                CH = 3.4707 exp 1.485 × 10 T b + 16.94SG                                              2/3


                                                              (2.124)  T MN = 370 − exp(6.52504 − 0.04945M  )
                                 −2
        (2.120)       −1.2492 × 10 T b SG     T −2.725 SG −6.798
                                           b
         where T b is in kelvin. The above equation was used to extend  (2.125)  T MA = 395 − exp(6.53599 − 0.04912M 2/3 )
         its application for hydrocarbons from C 6 to C 50 .
                                                              where T M is in kelvin. These equations are valid in the car-
                                           −3
            CH = 8.7743 × 10 −10  
 exp 7.176 × 10 T b + 30.06242SG  bon ranges of C 5 –C 40 ,C 7 –C 40 , and C 9 –C 40 for the P, N, and

                            −3
         (2.121)   −7.35 × 10 T b SG     T −0.98445 SG −18.2753  A groups, respectively. In fact in wax precipitation linear
                                     b                        hydrocarbons from C 1 to C 15 as well as aromatics are ab-
         where T b is in kelvin. Although this equation was developed  sent, therefore there is no need for the melting point of very
         based on data in the range of C 20 –C 50 , it can also be used  light hydrocarbons [64]. Equation (2.124) is for the melt-
         for lower hydrocarbons and it gives AAD of 2% for hydrocar-  ing point of n-alkylcyclopentanes. A similar correlation for
         bons from C 20 to C 50 . Most of the data used in the develop-  n-alkylcyclohexanes is given by Eq. (2.42) with constants in
         ment of this equation are from n-alkanes and n-alkyl mono-  Table 2.6. In Chapter 3, these correlations will be used to es-
         cyclic naphthenic and aromatic compounds. Estimation of  timate freezing point of petroleum fractions.
         CH weight ratio from other input parameters is possible  Won [79] and Pan et al. [63] also proposed correlations
         through Eq. (2.40) and Table 2.5. Once CH weight ratio is  for the freezing points of hydrocarbon groups. The Won






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