Page 69 - Applied Process Design For Chemical And Petrochemical Plants Volume II
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58                       Applied Process Design for Chemical and Petrochemical Plants

           n = total system pressure       (also see Equation 8 - 3)   Any non-volatile material in the mixture will be left in the
                                                                 still bottoms.
                                                                   The Hausbrand vapor-pressure diagram  [127, 1281  in
                                                                 Figure &40 is a useful approach for the steam distillation
           The steam required for the distillation is            calculation. This particular diagram was prepared for six
                                                                 organic compounds and the corresponding water vapor
           * = Ps  + Pirn                              (8-107)   pressure as (n - p,) for three system pressures of 760,300,
                                           (also see Equation 8-4)
                                                                 and 70 mm Hg versus temperature,
               * - Pim
           Ys  =-                                                where  M  = molecular weight of material
                  ll
                                                                        p  = partial pressure, mm Hg
             The steam required per mol of immiscible liquid vapor-     W = weight of material in vapor
           ized is                                                      N  = number of mols
                                                                       No  =i number of mols of non-volatile material present
           -=-=-  X-Pim   Ps                          (8- 107A)         y = mol fraction of material in vapor
            Ys
            Yim   F'im   Pim                                            x = system pressure, mm Hg
                                                                       pim = pure component vapor pressure of the immiscible
                                                                           liquid being distilled

             When the sum of the partial pressures of the steam and   Subscripts:
           the material distilled reach the system pressure, boiling
           begins and both components go overhead in the mol ratio     im  = immiscible liquid
           of their partial pressures. Upon condensation of the over-    s = steam
           head  mixture, the  condensate receiver will  contain two     1 =initial
           layers that can be separated by gravity.                     2  = remaining
             The weight ratio of steam to the immiscible liquid in the
           vapor is                                                The water curve intersects the particular organic com-
                                                                 pound  and at that point  the  temperature is  the  one at
                                                                 which the steam distillation can take place, because the
                                                       (8 - 108)
                                                                 partial pressures are additive at this point. For example,




























                                                                                Figure 8-40.  Hausbrand vapor-pressure dia-
                                                                                gram for various liquids and at three system
                                                                                steam  pressures. A  similar  diagram  can  be
                                                                                constructed  for  other  organidhydrocarbon
                                                                                systems. Used by permission, Ellerbee, R. W.,
                                                                                Chem. Eng. Mar. 4 (1 974), p. 108.
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