Page 531 - Elements of Chemical Reaction Engineering Ebook
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Sec. 8.7   Nonisothermal Multiple Chemical Reactions           501

                                The heat of reaction for reaction i must be referenced to the same species in the
                                rate, rG, by which AHRxrl is multiplied, that is,

                                          moles of j reacted in reaction i   joules "released" in reaction i
                        [-rrqIZ-AHRxr/l  =
                                                 volume - time      ]  [aes of j reacted in reactiz]

                                       = poules "released" in reaction i  1
                                                 volume. time
                                where the subscript  j  refers to the species, the subscript i to the particular reac-
                                tion, q is the number of independent reactions, and m is the number of species.
                                     Consider the following reaction sequence carried out in a PFR:

                                           Reaction 1:      A    k1  ,B                      (8-88)
                                           Reilction 2:     B    '>C                         (8-89)

                                The PFR energy balance becomes




                                where  AHRxlA  = [kJ/mol of A reacted in reaction 13 and   = kJ/mol
                                of B reacted in reaction 21.


                                   Example  8-11  Parallel  Reactions in a PFR with Heat Effects

                                   The following gas-phase reactions occur in a PFR:
                                                            k
                                            Reaction 1:   A  1_) B    -IlA = k1,CA         (E8-1 I .l)
                                            Rewtion 2:   2A   k2  >  C   -r2,  = k,,Ci     (E8- 1 1.2)

                                   Pure A is fed a1  a rate of  100 molls, a temperature of  150°C and a concentration of 0.1
                                   moll dm3 . Determine the temperature and flow rate profiles down the reactor.

                                   Additional information:
                                       AH,,,,  = J/mol of A reacted in reaction 1 = -20,000 J/mol
                                       AHRx2A .= J/mol of A reacted in reaction 2 = -60,000 J/mol

                                        CpA = 90 J/mol. "C    k,, = 10 expb [& - i)] s-1

                                        Cp, = 90 J/mol- "C    E, = 8000 cal/mol

                                                                                   A)]
                                        Cpc = 180 J/mol. "C   k2* = 0.09 exp [ E! (1 dm3
                                                                                 -
                                                                           R  300   T  mo1.s
                                        Ua=4000J/m3.s."C      E,=  18,00Ocal/mal
                                       T, = I0CI"C
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