Page 299 - Characterization and Properties of Petroleum Fractions - M.R. Riazi
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            AT029-Manual
                        AT029-Manual-v7.cls
  AT029-06
                                                        20:46
                                           June 22, 2007
                                                        Pressure, PSIA
                                                                     67 8 9 1,000
                                                                                       6 7 8 9 10,000
                                                                 4 500
                                    10  T1: IML  30  6. THERMODYNAMIC RELATIONS FOR PROPERTY ESTIMATIONS 279
                                               4 50
                                                  67 8 9100
                                                                                3,000
                                                               300
                                                                              2
                                                                                    4
                                   10     2                 2                              10
                                    9                                                       9
                                    8                                                       8
                                    7                                                       7
                                    6                                                       6
                                    5                                                       5
                                    4                                                       4
                                    3                                                       3
                                    2                                                       2
                                   1.0                        Temperature °F               1.0
                                                                500
                                    9                                                       9
                                    8                           450                         8
                                    7                                                       7
                                    6                                                       6
                                    5                           400                         5
                                    4                                                       4
                                    3                                                       3
                                    2                           300                         2
                                                                280
                                   0.1                          260                         0.1
                                                                240
                                    9                                                       9
                                    8                           220                         8
                                    7                                                       7
                                    6                           200                         6
                                    5                                                       5
                                    4                           180                         4
                               K =  y /x 3                      160                         3  K =  y /x
                                    2                           140                         2
                                                                120
                                   .01                          100                         .01
                                    9                                                       9
                                    8                                                       8
                                    7                           80                          7
                                    6                                                       6
                                    5                                                       5
                                                                60
                                    4                                                       4
                                    3                                                       3
                                                                40
                                    2                                                       2
                                                                20
                                  .001                                                      .001
                                    9                                                       9
                                    8                           0                           8
                                    7                                                       7
                                    6                                                       6
                                    5                                                       5
                                    4                           –20                         4
                                    3                                                       3
                                    2                                                       2
                                                                –40
                                 .0001                                                      .0001
                                    10    2  30  4 50  67 8 9 100  2  300  4 500  67 8 9 1,000  2  3,000  4  67 8 9 10,000
                                                        Pressure, PSIA         Heptane
                                                                        CONV. PRESS. 10,000 PSIA
                                                                                 ◦
                                FIG. 6.27—K i values of heptane. Unit conversion:  ◦ F = C × 1.8 + 32 psia =
                              14.504 × bar. Taken with permission from Ref. [28].
            where for ideal liquid and solid solutions γ  L  and γ  S  are  begins for a mixture (see Problem 6.29). Multicomponent --`,```,`,``````,`,````,```,,-`-`,,`,,`,`,,`---
                                                  i      i
                                                    L
            unity and the pure component fugacity ratio f /f  S  can be  SLE calculations become very easy once the stability analysis
                                                    i  i
                                                         S
            calculated from Eq. (6.155). For nonideal solutions, γ may  is made. From stability analysis consideration a component
                                                         i
                                               S
            be calculated from Eq. (6.153). However, δ calculated from  in a liquid mixture with mole fraction z i may exist as a pure
            Eq. (6.153) must be used for δ in Eq. (6.154). Equations  solid if the following inequality holds [17]:
            (6.208) and (6.209) can be used to construct freezing/melting        ˆ          S
                                              S L
            points or liquid–solid phase diagram (Tx x ) based on SLE  (6.210)  f i (T, P, z i ) − f (T, P) ≥ 0
                                                                                            i
                                                                        S
            calculations as shown in Chapter 9. For an ideal binary sys-  where f is fugacity of pure solid i. This equation is the ba-
                                                                        i
                     S L
            tem the Tx x diagram is shown in Fig. 6.32. Such figures  sis of judgment to see if a component in a liquid mixture
            are useful to determine the temperature at which freezing  will precipitate as solid or not. The answer is yes if the above
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