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36  Chapter 2: Kinetics and Ideal Reactor Models

                            (b) From the definition of space time given in Section 2.1, as in equation 2.3-2,

                                                             7  = v/q,                          (2.3-2)

                            This is the same result as for residence time  t  in  constant-density  flow, equation 2.4-8.
                            However, in this case, density is not constant through the PFR, and the result for r is
                            different from that for  t  obtained in (a).
                              Using equation 2.4-4 in integrated form, V = 1 FAodfAl(  -I*),  together with the stoi-
                            chiometry of the reaction, from which the total molar flow rate at any point is


                                                 Ft =  FA +FC,H, +FH2
                                                    = FA,(~ - .fA) +FAO~A  +FAO~A
                                                    =  F,,(l +  fA)
                            and the ideal-gas equation of state, from which the volumetric flow rate at any point is

                                                           q =  F,RTIP

                            where  R  is the gas constant, and the inlet flow rate is

                                                     qO  =  F,,RTIP  =  FA,RTIP

                            we obtain, on substitution into equation 2.3-2,
                                                                    1
                                                 7=     FAodfAl(-rA)   I(FA,RTIP)


                                                              (1 + fA)dfAl(l - fA)


                                                   = 0.99s

                            (c) T  >  t,  because  T,  based on inlet conditions, does not take the acceleration of the flowing
                            gas stream into account. The acceleration, which affects  t,  is due to the continuous increase
                            in moles on reaction.


       2.5 LAMINAR-FLOW REACTOR (LFR)

                            A laminar-flow reactor (LFR) is rarely used for kinetic studies, since it involves a
                            flow pattern that is relatively difficult to attain experimentally. However, the model
                            based on laminar flow, a type of tubular flow, may be useful in certain situations,
                            both in the laboratory and on a large scale, in which flow approaches this extreme (at
                            low Re). Such a situation would involve low fluid flow rate, small tube size, and high
                            fluid viscosity, either separately or in combination, as, for example, in the extrusion of
                            high-molecular-weight polymers. Nevertheless, we consider the general features of an
                            LFR at this stage for comparison with features of the other models introduced above.
                            We defer more detailed discussion, including applications of the material balance, to
                             Chapter 16.
                              The general characteristics of the simplest model of a continuous LFR, illustrated
                             schematically in Figure 2.5, are as follows:
                               (1) The flow through the vessel is laminar (LF) and continuous, but not necessarily
                                  at constant rate.
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