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9.2 Gas-Liquid Systems 241
                                  where the liquid-film mass transfer coefficient is defined by


                                                           'be  = DA&%                          (9.2-7)
                              (4) There is equilibrium at the interface, which is another way of assuming that there
                                  is no resistance to mass transfer at the interface. The equilibrium relation may
                                  be expressed by means of Henry’s law:

                                                           PAi  =  HACAi                        (9.2-8)

                                  where  HA  is the Henry’s law constant for species A.
                              The rate of mass transfer of A may also be characterized in terms of overall mass
                            transfer coefficients KAg and KA,  defined by

                                                        NA = KA&'A - 6~)                        (9.2-9)
                                                           = KA&~  - cA)                       (9.2-10)

                            where pi is the (fictitious) partial pressure of A in equilibrium with a liquid phase of
                            concentration CA,


                                                            Pi = HACA                          (9.2-11)
                            and, correspondingly, CL  is the liquid-phase concentration of A in equilibrium with a
                            gas-phase partial pressure of PA,

                                                            PA =HAC~                           (9.2-12)

                            KAs  and KAe may each be related to kAg  and kAo.  From equations 9.2-3, -6, and -9,

                                                          1
                                                         -= ‘+HA                               (9.2-13)
                                                         KAY    kg    kAC

                            and from equations 9.2-3, -6, and -10,
                                                         1  -    1  -   1
                                                        -  -  HAkAg  + kA,                     (9.2-14)
                                                        KA,
                              Each of these last two equations represents the additive contribution of gas- and
                            liquid-film resistances (on the right) to the overall resistance (on the left). (Each mass
                            transfer coefficient is a “conductance” and its reciprocal is a “resistance.“)
                              Special cases arise from each of equations 9.2-13 and -14, depending on the relative
                            magnitudes of kAg and k,,. For example, from equation 9.2-13, if kAg  is relatively large
                            so that Ilk,, << HAlkAe,  then KAs  (and hence  NA)  is determined entirely by kAe,  and
                            we have the situation of “liquid-film control.” An important example of this is the situ-
                            ation in which the gas phase is pure A, in which case there is no gas film for A to diffuse
                            through, and kAg --+  W. Conversely, we may have “gas-film control.” Similar conclu-
                            sions may be reached from consideration of equation 9.2-14 for  KAe.   In either case, we
                            obtain the following results:

                                              NA = kAe(PAjHA -  CA);  liquid-film control      (9.2-15)


                                               NA  =  kAg(pA   -  HA  CA);  gas-film   Control  (9.2-16)
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