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9.2 Gas-Liquid Systems 253

                            film, and as such is analogous to the Thiele modulus 4  in catalytic reactions (Chap-
                            ter 8).
                              This interpretation of Ha may be deduced from its definition. For example, for a  first-
                            order reaction, from equation 9.2-40,

                                          ~~2   =  62   kA   _  6  _  Vf kACAi
                                                  kAaicAi

                                                 e DA,    e=-        ai kAe cAi                (9.2-55)
                                                e maximum rate of reaction or flux in liquid film
                                              =  maximum rate of transport through liquid film

                            In equation 9.2-55, ai  is the interfacial area, for example, in m2 me3 (liquid), and  vf
                            is the volume of the liquid film. The rates are maximum rates because c,&  is the high-
                            est value of  CA  in the film (for numerator), and the form of the denominator is con-
                            sistent with CA  (bulk liquid) = 0, giving the largest possible driving force for mass
                            transfer.
                              Thus, if Ha (strictly, Ha2) >> 1, reaction occurs in the liquid film only, and if Ha or
                            Ha2 ==K 1, reaction occurs in bulk liquid. Numerically, these values for Ha may be set
                            at about 3 and 0.1, respectively.





                            Suppose pure CO, (A) at 1 bar is absorbed into an aqueous solution of NaOH  (B) at 20” C.
                            Based on the data given below and the two-film model, how should the rate of absorption
                            be characterized (instantaneous, fast pseudo-first-order, fast second-order), if  cu  = (a) 0.1
                            and (b) 6 mol L- 1 ?
                              Data (Danckwerts, 1970, p. 118, in part):  kA = 10,000 L  mol-’ s-l;  DA, = 1.8 X
                             lo-’  cm2  S-‘;  kAe = 0.04 cm  S-‘;  D,e  = 3.1 X  10-5cm2s-1;HA  = 36barLmoll’.


       SOLUTION

                            The chemical reaction (in the liquid phase) is

                                                CO,(g)  + 2NaOH(e)   --r Na,CO,   + H,O

                            Hence, b = 2.
                               Since a finite value of the rate constant kA   is specified, the reaction is not instantaneous.
                            The units given for  kA  indicate that the reaction is second-order, presumably of the form in
                            equation 9.2-50. To obtain further insight, we calculate values of Ha and  Ej,  from equations
                            9.2-54 and 9.2-53, respectively. For  Ej,  since the gas phase is pure CO,, there is no  gas-
                            phase resistance, and CAM  = PA/HA,  from equation 9.2-8, with pAi = pA(  = 1 bar). The
                            results for the two cases are given in the following table (together with values of E, as
                            discussed below)
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