Page 86 - Elements of Chemical Reaction Engineering 3rd Edition
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5a                                  Conversion and Reactor Sizing   Chap. 2

                        The space velocity (SV), which is defined as

                                                                                      (2-22)

                        might  at first sight be regarded as the reciprocal  of  the space time. However,
                        there is a difference in the two quantities'  definitions. For the space time, the
                        entering volumetric flow rate is measured at the entrance condition, while for
                        the  space  velocity  other conditions  are  often  used.  The  two  space  velocities
                        commonly used in industry are the liquid hourly and gas hourly space veloci-
                        ties,  LHSV  and GHSV, respectively. The  uO in the LHSV  is  frequently mea-
                        sured as that of a liquid at 60 or 75"F, even though the feed to the reactor may
                        be a vapor at some higher temperature. The uo in the GHSV is normally mea-
                        sured at standard temperature  and pressure (STP).
                             For reactions in which the rate depends only on the concentration of  one
                        species [i.e., -rA  = f(cA)],  it is usually convenient to report  -rA  as a function
                        of concentration rather than conversion. We can rewrite the design equation for
                        a plug-flow reactor  [Equation (2-16)] in terms of the concentration, CA, rather
                        than in terms of conversion for the special case when  u = uo .


                                                                                      (2-16)


                                                    FAO  = uO  'A0                   (2-23)
                        Rearranging Equation (2-10) gives us

                                                                                      (2-24)


                        For the special case when  u  = uo,




                                       when X  = 0, CA = CAO

                                       when X  = X, CA = CA
                        Differentiating yields

                                                       -dCA
                                                 dX=  -
                                                        cAO
                                                                                      (2-25)
            equation




        Valid only if  u  = uo                                                        (2-26)
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