Page 231 - Elements of Chemical Reaction Engineering 3rd Edition
P. 231

Chap. 4   Sumrnary                                             203

                                     2.  Pressure drop in isothermal reactors
                                        a.  Variable density with  E # 0:
                                                          P
                                                     Y=-
                                                         PO







                                                                                              (34-9)











                                        b.  Variable density  with E = 0 or EX* 1 and isothermal:

                                                              -- - (1 -aW)'"                 (s;4- IO)
                                                              PO
                                      3. For semibatch reactors, reactant B is fed continuously to a vat initially
                                        containing only A:

                                                              A-I-B  __j C

                                        a.  In terms of conversion:
                                                                  dX
                                                               N  -    = -                   (S4-11)
                                                                A        r*V
                                                                 '  dt
                                        b.  Rate law:


                                                                                             (S4-12)


                                                                I.'  = vo + U0t              (S4- 13)

                                                                                             (S4-14)


                                                                                             (S*4-15)

                                        Equations  (S4-11)  through  (S4-15)  are  combined  and  the  resulting
                                        equation is solved numerically for conversion as a function of  time.
                                        c.  In terms of  concentrations,
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