Page 187 - Essentials of physical chemistry
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Basic Chemical Kinetics                                                     149

            This is really an amazing mathematical trick because we should see that the two terms in N B would
                                                               k b t
            be part of a derivative of a product if only there was a factor of e , so why not multiply the whole
            equation by that factor? Now we can integrate both sides of the equation:
              ð           ð                             (k b  k a )t
                                                       e
                                           k b t
                                (k b  k a )t
                  k b t
                d(e N B ) ¼ k a N 0 e  dt ) e N B ¼ (k a N 0 )  þ C but N B ¼ 0at t ¼ 0, so we
                                                       (k b   k a )
                                        k a N 0 e (k a   k b )t
                      k a N 0                         k a N 0
                                 k b t
                    (k b   k a )         (k b   k a )  (k b   k a )
            have C ¼        and e N B ¼                    . Then collecting common factors we
                        k a N 0 e (k a   k b )t
                 k b t                k a N 0   k a N 0  (k b   k a )t
            have e N B ¼                    ¼          e       1 and after we divide both sides
                         (k b   k a )  (k b   k a )  (k b   k a )
               k b t
            by e ,we finally reach
                                              k a N 0      k a t   k b t
                                                    e     e    :
                                       N B ¼
                                            (k b   k a )
            That gives us a formula for N B at any time t > 0. When will the contents of tank B reach a

                                          dN B                                      dN B
            maximum?   We  need  to  set        ¼ 0  and  solve  for  t max N B .  Thus,  ¼
                                           dt                                        dt

              k a N 0  	   k a t   k b t                k a t   k b t
                       k a e  þ k b e  ¼ 0. Therefore k a e  ¼ k b e  ; now take the natural log of
             (k b   k a )

                                                              k a
            the whole equation, so ln k a   k a t ¼ ln k b   k b t or ln  ¼ (k a   k b )t. Thus, t max N B  ¼
                                                              k b

             ln  k a
               k b
                                  using the numerical values,
                   . Now find t max N B
            (k a   k b )
                                            0:693
                                          0      1
                                            3 days
                                          B      C
                                         ln B    C
                              k a         @ 0:693  A            8
                           ln                                ln
                                            8 days              3
                              k b
                   t max N B  ¼   ¼                    ¼               ¼ 6:7936 days:
                           (k a   k b )  0:693  0:693           8   3
                                                         0:693

                                      3 days    8 days         24 days
            With this information we can find out how much water=solution is in tank B at that time:

                                             0:693
                                                   (1000 gal)
                      k a N 0      k a t   k b t     3 days  h  0:693        0:693   i
                             e     e                         e  ð  3 Þ(6:7936)    e  ð  8 Þ(6:7936)  ,
                    (k b   k a )            0:693     0:693
               N B ¼                    ¼
                                           8 days     3 days
            and so N B (max) ¼ ( 1600 gal) ( 0:346975) ¼ 555:16 gal. We might as well calculate the con-
            tents of tank A and tank C at this time, assuming the outlet valve of tank C is closed.
                              0:693
              N A ¼ (1000 gal)e   ð 3 days Þ(6:7936 days)  ¼ 208:19 gal, so assuming conservation of the initial 1000 gal
            (neglecting evaporation) we can calculate the volume in tank C as whatever is not in tank A or
            tank B. The volume in tank C ¼ (1000 208.19 555.16) ¼ 236.65 gal at t ¼ 6.7936 days. We also
            realize that eventually all the solution will end up in tank C with tanks A and B completely empty.
            If this was a problem in nuclear decay, we might have so few individual atoms starting from a
            number like 1000 atoms that we would have to round the values of N A , N B , and N C to integer values
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