Page 38 - Applied Process Design For Chemical And Petrochemical Plants Volume II
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Distillation                                           27


                                                      pB  XB
             Temp"C  (PR-PT)  (JG-P~T) XR        . = B y   z
               80       480     480   1.0    0      1.0    0
               90       590     350   0.593   0.407   0.780   0.220
               100      770     210   0.273  0.727  0.474   0.526
               110     1,000     20   0.0    0.980  0.0457  0.954   11w
               111.5   1,000      0   0.0    1.0    0.0    1.0

               Plot values of xg, XT, YT, and yg on Figure 8-18.
                                                                  p  100'
             Example 86: Repeat Example 8-5 using K-values. Refer   ui
                                                                  K
             to basis of Example 8-4.                             z
                                                                  a
             Using the data from Reference 59 (pp. 221, and 233):   90'

             Temp.           Re1 .
                     KT  Vol., ag/~* Kg =UKT  1 - KT  (Kg - KT)
             --
               "C
               80    0.37    2.65      0.981    0.63     0.611
               90    0.33    2.48      1.314    0.47     0.784
              100    0.73    2.39      1.745    0.27     1.015
              110    0.97    2.35      2.28     0.03     1.31       70'
              111.5  1.0     2.35      2.35     0.0      1.35           0   0.1   0.2   0.3   OA   0.5   0.6   0.7   0.8   0.9   1.0
             *Read from chart [59].
                                                                                         MOL FRACTION BENZENE
                                                                                         MOL FRACTION TOLUENE
             XB = 1 - KT/
               (KB - KT)    XT   1 - Xg   YB = KBXB    YT = KTXT   Figure  8-20.  Boiling  point  diagram  for  benzene-toluene  mixture
                                                                   using K values, total pressure 760 mm Hg; for Example 8-6.
               *1.031         0.0          80.981        0.0
                0.60          0.40          0.789        0.212
                0.266         0.734         0.464        0.535
                0.0229        0.977         0.0523       0.946
                0.0            1 .o         0.0          1 .o
                                                                      1 .o
             *Note: If graphs could be read close, these values would be equal to 1 .O.
                                                                                                based
                                                                                             Cuwe
                                                                                           x-y
                                                                                           x-y  Cuwe based on
                                                                                                    on
             Procedure                                                0.9                  Boillng Point Diagram
                                                                                                 Diagram
                                                                                           Boillng
                                                                                              Point
               1. Read K value for toluene from tables or charts.     0.8
               2. Read CY. values for benzene/toluene from Reference 59.
               3. Calculate K (benzene) from: ag/~ KB/KT           6   0.7
                                                =
               4. Calculate Xbenzene:                              3
                                                                   f   0.6
                  YB'GXB                                           fi
                                                                      0.5
                  YT = KT  xT                                      5
                  Z1.0 = KBXB + KTXT = KBXB + KT (1 - XB)          $   0.4
                                                                   U
                       XB (% - KT) +KT                             d
                                                                      0.3
                   XB = (1 - KT)/(KB - KT)
                                                                      0.2
               5. calculate Ybemene: yB =   XB
               6. Plot boiling point diagram, see Figure 8-20.
               7. Plot x-y diagram, see Figure 8-21.                  0.1
                                                                       0   V
                                                                                                              1  1
                                                                                                1  1
                                                                                                                  1  1
                                                                                                         1  1
                                                                                       1  1
                                                                                            1  1
                                                                                                     1  1
             Example &?:  Flash Vaporization of a Hydrocarbon            0   0.1  1  1   0.2   0.3   0.4   0.5   0.6   0.7   0.8   0.9   IO
             Liquid Mixture
                                                                                       MOL FRACTION BENZENE IN LIQUID
               What fraction of a liquid mixture containing 10 mole%   Figure 8-21. x-y  diagram for benzene in benzene-toluene mixture,
             propane, 65%  n-butane and 25%  n-pentane would  be   760 rnrnHg total pressure, based on K-values, Example 8-6.
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