Page 134 - Elements of Chemical Reaction Engineering 3rd Edition
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106                                  Rate Laws and Stoichiometry   Chap. 3

                           Example 3-9  PFR Mole Balances in Terms of Molar Flow Rates
                           Reconsider the elementary gas reaction discussed in Example 3-8.

                                                   N,O,        2N0,
                                                      A -
                                                              2B
                                                        +
                           The reaction is to be carried out isothermally (T = T,) and isobarically (P = Po) in
                           a PFR. Express the rate law and mole balances in terms of  the molar flow rates.

                           Solution

                                Mole balance:                                        (E3-9.1)


                                                                                     (E3-9.2)




                                Rate law:                                            (E3-9.3)


                                                        ‘A  - ‘B
                                Stoichiometry:         - --
                                                        -1   2
                                             Then
                                                       r,  = -2r,                    (E3-9.4)

                                Combine:
                           Using Equation (3-45) to substitute for the concentrations of A and B when  T = To
                           and  P  = Po, Equation (E3-9.3) becomes
                                                                $$$I
                                              -rA=kd [ C,, (:)   - --                (E3-9.5)



                           where the total molar flow rate is just the sum of the flow rates of A and B:

                                                      F,=  FAi-FB                    (E3-9.6)

                           and the total concentration of the entrance to the reactor (Po, To ) is calculated from
                           the equation

                                                             PO
                                                       c,, = -                       (E3-9.7)
                                                            RTO
                           Combining Equations (E3-9.5) and (E3-9.6), we obtain
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