Page 130 - Elements of Chemical Reaction Engineering 3rd Edition
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1 02                                Rate Laws and Stoichiometry   Chap. 3

                            (c)   Assuming  the reaction is elementary, express the rate of  reaction  solely  as a
                                function of conversion  for a flow system and for a batch  system.

                            Solution

                                                      A e
                                                               2B
                            At equilibrium the concentrations of the reacting species are related  by  the relation-
                            ship dictated by thermodynamics  [see Equation (3-10) and Appendix C]

                                                                                     (E3-8.1)

                           (a) Batch system-constant volume, V  = V, . See Table E3-8.1.


                                              TABLE E3-8.1.  STOICHIOMETRIC TABLE
                                  Species   Symbol    Initial   Change     Remaining
                                   N*O,      A      NAO       -NAoX     NA = NAo (1 - X)
                                   NO*       B      0         +2NA0X    NB = 2NA0X
                                                    Nro  = NAO          NT  = NTO  + NAdr


                                                1
                           For batch systems  Ci = Ni V ,
                                                                                     (E3-8.2)



                                                                                     (E3-8.3)


                                           YAOPO  -
                                      c,,  = -                  atm)
                                                -
                                            RT,    (0.082 atm . dm3/grnol' K)(340 K)
                                         = 0.07174 mol/dm3
                           At  equilibrium  X  = X,  and  we  substitute  Equations  (E3-8.2)  and  (E3-8.3)  into
                           Equation  (E3-8.1),






                                                                                    (E3-8.4)

                           We will use POLYMATH to solve for the equilibrium conversion and let xeb repre-
                           sent  the  equilibrium  conversion  in  a  constant-volume  batch  reactor.  Equation
                           (E3-8.4) written in POLYMATH format becomes
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