Page 67 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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            AT029-Manual
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                                           August 16, 2007
                                                          16:6
                                           2. CHARACTERIZATION AND PROPERTIES OF PURE HYDROCARBONS 47
            parameter and SG represents the size parameter. Therefore,
            in Eq. (2.31) one can replace parameters A and B by T b and  parameters and transport properties are discussed in Chap-
                                                                  ters 5, 6, and 8. It is shown by various investigators that the
            SG. However, it should be noted that T b is not the same as  ratio of T b /T c is a characteristic of each substance, which is
            parameter A and SG is not the same as parameter B, but it  related to either T c or T b [36, 43]. This ratio will be used to
            is their combination that can be replaced. There are many  correlate properties of pure hydrocarbons in Section 2.3.3.
            other parameters that may represent A and B in Eq. (2.31).  Equation (2.31) can be written once for T c in terms of V and I
            For example, if Eq. (2.25) is applied at a reference state of T 0  and once for parameter T b /T c . Upon elimination of parameter
            and P 0 , it can be written as                        V between these two relations, a correlation can be obtained
                                                                  to estimate T c from T b and I. Similarly through elimination
                                                                  of T c between the two relations, a correlation can be derived
            (2.32)          V T 0 ,P 0  = f 3 (A, B, T 0 , P 0 )
                                                                  to estimate V in terms of T b and I [42].
                      is the molar volume of the fluid at the reference  It should be noted that although both density and refrac-
            where V T 0 ,P 0
            state. The most convenient reference conditions are tempera-  tive index are functions of temperature, both theory and ex-
            ture of 20 C and pressure of 1 atm. By rearranging Eq. (2.32)  periment have shown that the molar refraction (R m = VI )is
                    ◦
            one can easily see that one of the parameters A or B can be  nearly independent of temperature, especially over a narrow
            molar volume at 20 C and pressure of 1 atm [28, 36, 42].  range of temperature [38]. Since V at the reference tempera-
                            ◦
              To find another characterization parameter we may con-  ture of 20 C and pressure of 1 atm is one of the characteriza-
                                                                          ◦
            sider that for nonpolar compounds the only attractive force  tion parameters, I at 20 C and 1 atm must be the other char-
                                                                                     ◦
            is the London dispersion force and it is characterized by fac-  acterization parameter. We chose the reference state of 20 C
                                                                                                                  ◦
            tor polarizability, α, defined as [38, 39]             and pressure of 1 atm because of availability of data. Simi-
                                                                  larly, any reference temperature, e.g. 25 C, at which data are
                                                                                                  ◦
                              3       M     n − 1
                                              2
            (2.33)     α =        ×      ×   2                    available can be used for this purpose. Liquid density and re-
                                                                  fractive index of hydrocarbons at 20 C and 1 atm are indicated
                            4π N A    ρ     n + 2                                              ◦
            where                                                 by d 20 and n 20 , respectively, where for simplicity the subscript
              N A = Avogadro’s number                             20 is dropped in most cases. Further discussion on refractive
              M = molecular weight                                index and its methods of estimation are given elsewhere [35].
               ρ = absolute density                                From this analysis it is clear that parameter I can be used
               n = refractive index                               as one of the parameters A or B in Eq. (2.31) to represent the
            In fact, polarizability is proportional to molar refraction, R m ,  size parameter, while T b may be used to represent the energy
            defined as                                             parameter. Other characterization parameters are discussed
                                  M     n − 1
                                          2                       in Section 2.3.2. In terms of boiling point and specific gravity,
            (2.34)         R m =     ×                            Eq. (2.31) can be generalized as following:
                                         2
                                  ρ     n + 2
                                                                                            b
                                                                 (2.38)               θ = aT SG c
                                                                                           b
                                      M
            (2.35)                V =                             where T b is the normal boiling point in absolute de-
                                      ρ
                                                                  grees (kelvin or rankine) and SG is the specific gravity at
                                                                  60 F(15.5 C). Parameter θ is a characteristic property such as
                                                                          ◦
                                                                    ◦
                                     2
                                    n − 1
            (2.36)               I =                              molecular weight, M, critical temperature, T c , critical pres-
                                     2
                                    n + 2                         sure, P c , critical molar volume, V c , liquid density at 20 C,
                                                                                                                 ◦
            in which V is the molar volume and I is a characterization  d 20 , liquid molar volume at 20 C and 1 atm, V 20 , or refrac-
                                                                                            ◦
            parameter that was first used by Huang to correlate hydrocar-  tive index parameter, I,at20 C. It should be noted that
                                                                                            ◦
            bon properties in this way [10, 42]. By combining Eqs. (2.34)–  θ must be a temperature-independent property. As mentioned
            (2.36) we get                                         before, I at 20 C and 1 atm is considered as a character-
                                                                              ◦
                                                                  istic parameter and not a temperature-dependent property.
                      R m   actual molar volume of molecules
            (2.37)  I =  =                                        Based on reported data in the 1977 edition of API-TDB, con-
                      V    apparent molar volume of molecules
                                                                  stants a, b, and c were determined for different properties
            R m , the molar refraction, represents the actual molar volume  and have been reported by Riazi and Daubert [28]. The con-
            of molecules, V represents the apparent molar volume and  stants were obtained through linear regression of the loga-
            their ratio, and parameter I represents the fraction of total  rithmic form of Eq. (2.38). Equation (2.38) in its numerical
            volume occupied by molecules. R m has the unit of molar vol-  form is presented in Sections 2.4–2.6 for basic characteri-
            ume and I is a dimensionless parameter. R m /M is the specific  zation parameters. In other chapters, the form of Eq. (2.38)
            refraction and has the same unit as specific volume. Parame-  will be used to estimate the heat of vaporization and trans-
            ter I is proportional to the volume occupied by the molecules  port properties as well as interconversion of various distil-
            and it is close to unity for gases (I g = 0), while for liquids it  lation curves. The form of Eq. (2.38) for T c is the same as
                                          ∼
            is greater than zero but less than 1 (0 < I liq < 1). Parameter  the form Nokay [44] and Spencer and Daubert [45] used to
            I can represent molecular size, but the molar volume, V,isa  correlate the critical temperature of some hydrocarbon com-
            parameter that characterizes the energy associated with the  pounds. Equation (2.38) or its modified versions (Eq. 2.42),
            molecules. In fact as the molecular energy increases so does  especially for the critical properties and molecular weight,
            the molar volume. Therefore, both V and I can be used as two  have been in use by industry for many years [2, 8, 34, 46–56].
            independent parameters to characterize hydrocarbon proper-  Further application of this equation will be discussed in
            ties. Further use of molar refraction and its relation with EOS  Section 2.9.
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