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88                                                       Chapter 3

                The total mole balance is not an independent equation because by adding the
           component balances  and then  substituting  Equations  3.4  to  3.8  into  the  sum will
           yield the total mole balance,

           n^ + ms  =m 2  +ni4                                          (3.9)

                If  you decide  to use  the  total balance, then you must  eliminate  one  of the
            equations from  3.4  to  3.8, given  above. You may eliminate  any  one  of  the  equa-
           tions.  The equation eliminated will depend on the particular problem. Even if the
           total balance is not an independent equation, it still must be satisfied  and could be
           use as a check on your computations.

           Energy Balances
           The macroscopic energy balance is used whenever energy changes occur, particu-
            larly  energy exchange with the  surroundings. Energy exchange occurs  frequently
           because of the need to cool or heat process streams and to transfer  liquids, gases or
            solids  from  one  process  unit  to  another.  Energy  exchange  usually  occurs  more
            frequently than separation and chemical reaction.  The energy balance is given by

                v 2
            Ah + — + gAz = Q-W                                         (3.10)
                2g

            which  states that the change in enthalpy in the process unit must be  compensated
            for  by  a change in kinetic  energy, potential  energy,  heat  transferred  into the sys-
            tem,  and work done by the  system.  In  many processes, the kinetic and potential
            energy changes are small when compared to the magnitude of the other terms and
            may be neglected.

            Rate Equations
            All physical and chemical transformations  take time.  Some physical phenomena,
            such as the vaporization at a boiling liquid surface,  occurs very rapidly and  for all
            practical  purposes  are  instantaneous.  Also,  some  chemical  reactions,  such  as
            combustion reactions,  are  very rapid,  but mass transfer  and  many  chemical reac-
            tions  are  very  slow  by  comparison.  For  such  phenomena  to  occur  to  the  extent
            desired requires allowing sufficient  time, which is achieved by allowing sufficient
            equipment  volume  or  surface  area.  Rate  equations,  then,  are  necessary  to  deter-
            mine  equipment  sizes.  For  example,  the  well-known  expression  for  the  rate  of
            heat transfer,

                                                                        (3.11)
            Q = UA(At) LM




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