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452                       Steady-State Nonisothermal Reactor Design   Chap. 8

                                           TABLE 8-2~.  ADIABATIC  PFR/PBR ALGORITHM
                                   The elementary reversible gas-phase reaction


                              IS carried out in a PFR in which pressure drop is neglected and pure A enters the reactor.

                               Mole balance:                                       (T8-2.1)


                               Rate law:                                           (T8-2.2)



                                   with                                            (T8-2.3)


                                                                                   (T8-2.4)


                               Stoichiometry:       Gas,  E = 0, P = Po






                                                              TO
                                                      c, = CA0X -                  (T8-2.6)
                                                              T
                                                -r,  = kCAo [ (1 -X)-- 4:          (T8-2.7)
                               Combine:
                                                                    -

                              Energy balance:
                                   To relate temperature and converslon we apply the energy balance to an adia-
                                   batic PFR. If  all species enter at the same temperature,  To = To.
                                   Solving Equation (8-50) to obtain the function of conversion yields
                                           T= X[-AH;;,(T,)]+~,,E,,T,+X  Aep',TR
                                                                                   (T8-2.8)
                                                      C@,~,,+XA~,

                                   If pure A enters and Atp = 0, then

                                                                                   (T8-2.9)

                                   Equations  (T8-2.1) through  (T8-2.9) can easily be solved using either Simp-
                                   son's rule or an ODE solver.
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