Page 265 - Introduction to chemical reaction engineering and kinetics
P. 265

246  Chapter 9: Multiphase Reacting Systems

                           The value of cn in the bulk liquid is the largest value of cn that can influence the rate of
                           reaction, and may be designated  $irnax. From equation (A), with 6  = 0, and  S,  =  D,elk,e,
                           equation  9.2-7,

                                                               KAgDAtbpA
                                                    CB,max  =                                 (9.2-23)
                                                            DBt kA,  -KA~HA  1
                                                               (
                                                          =  k&‘PdkBe
                           if we use the condition for gas-film control, from equation 9.2-13, l/k,, >> HA/k,,  or
                           kA, > > HA kAg,  SO that KAg = kAg,   together with equation 9.2-21 to eliminate  DA,  D,,,
                           and  k,,  in favor of k,,.
                             To obtain  (-rA)  for gas-film control, we may substitute  cn,max  from equation 9.2-23
                           into equation 9.2-22, and again use  k,,  >>  HAkAg,   together with equation 9.2-21:

                                                                                              (9.2-24)
                                                   (-rA)  = kAgPA;   CB   z CB,max
                           Thus, when  cn 2 crsrnax,  the rate (-TA)  depends only on PA.

                             This result also has implications for (-?-A)  given by equation 9.2-22. This equation
                           applies as it stands only if cB  I c~,~~. For higher values of  cn,  equation 9.2-24 governs.





                           What is the form of equation 9.2-22 for liquid-film control?


      SOLUTION
                           For liquid-film control, there is no gas-phase resistance to mass transfer of A. Thus, in
                           eqUEitiOU 9.2-14,  IlkA,  >> l/HAkAg,  and  KAe = kAe,  so that equation 9.2-22b may be
                           written

                                                  (-rA) =                                     (9.2-25)


                           9.2.3.3.2. Fast reaction. If chemical reaction is sufficiently fast, even though not instan-
                           taneous, it is possible for it to occur entirely within the liquid-film, but not at a point or
                           plane. This case is considered as a special case of reaction in both bulk liquid and liquid
                           film in Section 9.2.3.4. In this situation,  NA   =  (-TA).

                           9.2.3.3.3. Enhancement factor E. For reaction occurring only in the liquid film,
                           whether instantaneous or fast, the rate law may be put in an alternative form by means
                            of a factor that measures the enhancement of the rate relative to the rate of physical
                            absorption of A in the liquid without reaction. Reaction occurring only in the liquid
                            film is characterized by cA +  0 somewhere in the liquid film, and the enhancement
                            factor  E  is defined by



                                                       rate of reaction or flux of A
                                    E =
                                         maximum rate of mass transfer of A through the liquid film
                                       = (-rdlkAt(CAi  - cA) = (-rA)/kA&Ai
                                                                                             (9.2-26)      /
   260   261   262   263   264   265   266   267   268   269   270