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                        AT029-Manual-v7.cls
  AT029-06
                                           June 22, 2007
            AT029-Manual
                                               6. THERMODYNAMIC RELATIONS FOR PROPERTY ESTIMATIONS 289



                                                                   FIG. 6.39—Prediction of Z factor of propane at 30 bar from LJ
                                                                 EOS with parameters from different methods. Taken with per-
              FIG. 6.37—Prediction of Z factor for methane at 30 bar from
            vdW EOS using parameters from velocity of sound data. Taken  mission from Ref. [44].
            with permission from Ref. [44].
                                                                  6.9.2.3 RK and PR EOS Parameters—Property
            in Table 6.17. Errors for calculated Z values with use of LJ  Estimation
            parameters from different methods are also given in this ta-  To further investigate the possibility of using velocity of sound
            ble. Van der Waals EOS parameters determined from velocity  for calculation of PVT and thermodynamic data, RK and PR
            of sound are given in Table 6.18 and predicted Z values for  EOS parameters were determined for both gases and liquids
            methane and ethane are shown in Figs. 6.37 and 6.38, re-  through velocity of sound data. Using parameters defined in
            spectively. Predicted Z factor for propane from CSLJ EOS  Table 6.1 for calculation of γ , V, and (∂P/∂V) T and substi-
            (Eq. 5.96) is shown in Fig. 6.39. Results presented in Ta-  tuting them into Eq. (6.216), velocity of sound, c, can be es-
            bles 6.15–6.17 and Figs. 6.36–6.39 show that EOS parame-  timated. For both RK and SRK equations the relation for c
            ters determined from velocity of sound provide reliable PVT  becomes
            data and may be used to calculate other thermodynamic
            properties.                                           2         V 2     RT      a(2V + b)
                                                                  c RK,SRK  =−  −        +
                                                                                            2
                                                                            M     (V − b) 2  V (V + b) 2
                                                                                          2                       −1
                                                                           R       a 1        ig     Ta 2   V

                                                                     − T       −          × C − R −      ln
                                                                                              P
                                                                         V − b   V + bV               b    V + b
                                                                                  2
                                                                  (6.240)
                                                                  and for PR EOS the relation for c becomes

                                                                            V 2     RT        2a(V + b)
                                                                      2
                                                                     c PR  =−   −         +
                                                                                                       2 2
                                                                                              2
                                                                            M     (V − b) 2  (V + 2bV − b )
                                                                                      R         a 1
                                                                                                         2
                                                                               − T       −
                                                                                    V − b  V + 2bV − b 2
                                                                                             2
             FIG. 6.38—Prediction of Z factor for ethane at 100 bar from                                √     −1 ⎤
                                                                                           Ta 2
                                                                                   ig
            vdW EOS using parameters from velocity of sound data. Taken  (6.241)  × C − R − √  ln  V + b −  √ 2b  ⎦
                                                                                   P
            with permission from Ref. [44].                                               2 2b    V + b +  2b
                             TABLE 6.16—The Lennard–Jones parameters from the velocity of sound data and other sources.
                                   Velocity of sound         Second virial coefficient a     Viscosity data a
                  Compound   ε/k B ,K  σ, ˚ A  %AAD for Z  ε/k B ,K  σ, ˚ A  %AAD for Z  ε/k B ,K  σ, ˚ A  %AAD for Z
                  Methane    178.1    3.97     0.8       148.2   3.817       4.0      144.0   3.796      4.7
                  Ethane     300.0    4.25     0.5       243.0   3.594       3.0      230.0   4.418      3.4
                  Propane    350.0    5.0      1.1       242.0   5.637      11.5      254.0   5.061      8.0
                  Taken with permission from Ref. [44].
                  a The LJ parameters are used with Eq. (5.96) to calculate Z. The LJ parameters from the second virial coefficient and viscosity are taken from
                  Hirschfelder et al. [56]. k B is the Boltzman constant (1.381 × 10 −23  J/K) and 1 ˚ A = 10 −10  m.
                                    TABLE 6.17—The van der Waals constants from the velocity of sound data.
                                                Velocity of sound               Original constants a
                            Compounds    a × 10 −6   b      %AAD for Z   a × 10 −6   b      %AAD for Z
                            Methane     1.88583    44.78       1.0      2.27209    43.05       0.8
                            Ethane      3.84613    57.18       1.8      5.49447    51.98       2.4
                            Propane     8.34060    90.51       1.4      9.26734    90.51       1.5
                                                           6
                                                               2
                                                                            3
                            Taken with permission from Ref. [44]. a is in cm /mol · bar and b is in cm /mol.
                            a From Table 5.1.
                                                                                                                      --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---








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