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102    Single Reactions in Continuous Isothermal Reactors

                      continuous reactor, we make three moles of product for each mole of reactant fed into the
                      reactor so that the volumetric flow rate out of the reactor u  would be three times the flow
                      rate into the reactor uO,
                                                       v =  3v,
                      In a tubular reactor of constant diameter the velocity  u  when the reaction has gone to
                      completion is three times tbe inlet velocity  uO,
                                                       u  =  34
                      We call this situation  variable density, *and  the previous equations clearly do not describe
                      this situation because v, t,  and u  in these equations depend on the conversion.
                           For ideal gases the mole densities do not change if the reaction produces more or less
                      moles of product than the reactants. However, the mass density of the gas mixture changes,
                      and this causes the volumetric ilow  rate and velocity of gases through the reactor to change
                      as the conversion increases.
                           For the batch reactor we saw in the previous chapter that by switching from  CA  as
                      the composition variable to fractional conversion X, we could easily write the differential
                      equation to be solved for compositions versus time. We prefer to use concentration units
                      whenever possible, but, if the density is a function of composition, concentrations become
                      cumbersome variables, and we must switch to another designation of density such as the
                       fractional conversion X.


                       CSTR

                       For the CSTR we begin with the mass-balance equation we derived before we substitute
                       for concentration
                                                dN,
                                                J  =  Fjo  -  Fj  +  Vvjr
                                                 dt
                       which for reactant A  in steady state becomes
                                                  FAN   -  FA  -  Vr = 0
                       Now since the molar flow rate of  A  varies with conversion as
                                                   FA  =  FA,(~   -  X)
                       we can write this mass-balance equation as

                                               FAN   -  FA  =  F,J~X  =  Vr(X)
                       In steady state this equation can be rearranged to become






                       While this equation is correct for the steady-state CSTR with variable density, it does not
                       give a correct description of the transient CSTR for variable density because NA  (meaning
                       the number of moles of species A  in the reactor) is not given by the preceding expression
                       unless the density is constant.
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