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Sec, 2.3   Applications of the  Design Equations for. Continuous-Flow Reactors   41

                               each of  the concentrations  can be expressed as a function of  the conversion X
                               (see Chapter 3); consequently,  -rA  can be expressed as a function of  X.
                                    Ii particularly  simple  functional  dependence,  yet  one  that  occurs  on
                               many  occasions,  is -rA  = kCAo(1  - X). For  this  dependence,  a  plot  of  the
                               reciprocal  rate of reaction  (-l/rA)  as a function of  conversion yields a curve
                               similar to the one shown in Figure 2- 1 I where






                               To  illustrate  the  design  of  a  series  of  reactors,  we  consider  the  isothermal
                               gas-phase decomposition reaction

                                                         A  __j B+C
                               The laboratory  measurements  given in Table 2-1  show the chemical  reaction
                                rate  as  a  function of  conversion. The temperature  was  300°F (422.2  K),  the
                                total pressure  10 atm (1013 kPa),  and the initial charge an equimolar mixture
                                of A and inerts.

                                                         ‘TABLE 2-1  RAW DATA
                                                          X      -rA  (mol/dm3 . s)
                                                         0.0         0.0053
                                                         0.1         0.0052
               If we know  -rA as a                      0.2         0.0050
                 function of X, we                       0.3         0.0045
                     can size any                        0.4         0.0040
                      isothermal
                  reaction system.                       0.5         0.0033
                                                         0.6         0.0025
                                                         0.7         0.0018
                                                         0.8         0.00125
                                                         0.85        0.00100


                                     ‘The rate data in Table 2- 1 have been converted to reciprocal rates,  1 I - rA
                                in Table 2-2, which are now  used to arrive at the desired plot of  ll-rA  as a
                                function of X, shown in Figure 2-1. We  will use  this  figure to illustrate  how
                                one can  size each of  the reactors  in  a number of  different reactor  sequences.
                                The volumetric feed to each reactor sequence will be 6.0 dm3/s. First, though,
                                some initial conditions should be evaluated. If  a reaction is carried out isother-
                                mally, the rate is usually greatest at the start of  the reaction when the concen-
                                tration  of  reactant  is  greatest  [i.e.,  when  there  is  negligible  conversion
                                (X zz O)].  Hence (1 / - rA) will be small. Near the end of the reaction, when the
                                reactant concentration  is small  (i.e.,  the conversion is large), the reaction  rate
                                will  be  small.  Consequently,  (l/-rA)  is  large.  For  irreversible  reactions  of
                                greater than zero-order,
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