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Reactor Design                                                   369


            STIRRED-TANK REACTOR SELECTION

            The  operating mode of a stirred-tank reactor may be  either continuous or batch.
            A  STR  consists  of  a vessel to  contain the reactants,  a heat  exchanger,  a mixer,
            and  baffles  to  prevent  vortex  formation  and  to  increase  turbulence,  enhancing
            mixing.
                To evaluate and select a STR, consider the following  factors:

            1. mixing
            2. heat transfer
            3. jacket pressure drop
            4. cleaning

                Sufficient  power  must  be  supplied  to  the  liquid  to  approach  the  ideal
            model  of  a  thoroughly-mixed  reacting  system.  Inadequate  mixing  results  in  a
            longer average residence time and thus a larger reactor volume than for the ideal
            model.  Designing  a  mixing  system  requires  selecting  and  sizing  the  impeller,
            baffles,  and electric  motor.  For  a preliminary  design,  all  that  is  necessary  is  to
            estimate the mixer power.
                An  important  consideration  when  sizing  a  STR  is  heating  or'cooling  the
            reactor  contents.  There  are  several heat  exchangers,  which  are  classified  as  ei-
            ther  an  internal  or  external  heat  exchanger.  The  internal  heat  exchangers  are
            immersed directly into the reacting  liquid and consist of  spiral coils, harp coils,
            and hollow  or plate baffles.  We  will  only  consider  spiral  coils  when  designing
            an STR.
                The external heat exchanger may either be a jacket or a she 11-and-tube heat
            exchanger. For  the  latter, the reactor  contents circulate through an external  flow
            loop  containing  the  heat  exchanger.  The jacket  types,  as  illustrated  in  Figure
            7.2,  consist of  the simple jacket -  with or without a spiral baffle  or nozzles for
            promoting turbulence -  the partial pipe coil, and the dimple jacket.  The simple
            jacket  consists  of  an  outer  cylinder  enclosing  part  of  the  reactor.  A  heat-
            transfer  fluid  flows  in the annular area surrounding the reactor, as shown in Fig-
            ure 7.2. If the heat-transfer  rate is limited by the jacket heat-transfer  coefficient,
            then increase the turbulence in the jacket by using a spiral baffle  or nozzles.  The
            spiral baffle  is wound around and welded to the reactor.  The  baffle  channels the
            fluid  from  the jacket entrance  to the jacket  exit.  Channeling the  fluid  increases
            its  velocity  and  turbulence,  resulting  in  a  higher  heat  transfer  coefficient.  The
            partial pipe  coil  is  formed  by  cutting  a pipe  along  its  longitudinal  axis.  Then,
            the  coil  is  wrapped  around  the  reactor  in  a  helix  and  welded  onto  the  reactor
            shell.  The  dimple jacket  consists  of hemispherical  dimples pressed  into  a thin
            plate,  which  is  then  wrapped  around  and  welded  onto  the  reactor.  The jacket
            area  covers  about  80%  of  the  reactor  surface,  consisting  of  a bottom  elliptical
            head and a cylindrical shell.





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