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                    62                               3. Heterogeneous Processes and Reactor  Analysis


                      The rate coefficient is almost always dependent on temperature. However, it can be influ-
                    enced by total pressure, in both gas and liquid systems, plus ionic strength and solvent in liq-
                    uid systems. Following Fogler (1999), in the present book, the rate coefficient is considered
                    to be a function of only temperature, assuming that the effect of other variables is much less.
                    ement ang Reactor level—Catalyst plus r eactor arr

                    The principal difference between homogeneous and heterogeneous reaction rates is that the
                    , latter is based on mass, v or more rarely on the area of the solid and not on the fluid- olume,
                    phase volume or reactor volume. The reactor volume or liquid-phase volume is of second-
                    ary significance in heterogeneous reactions since the reaction takes place on the solid rather
                    than throughout the reactor volume. Moreover, the mass of the solid is usually used instead
                    .  of the solid volume or surface, because it is the most easily measured property
                      However, for purposes of mass balance in reactors, the following rates hae to be also v
                    considered: the rate of reaction per unit v olume of the fluid phase (  r ) and per unit volume u
                    of reactor (  R ), defined as follo 1972): v ws (Le enspiel,
                                                        1d  N
                                                   r                                   (3.16)
                                                    u
                                                       V  L  t d
                                                        1d  N
                                                    R                                  (3.17)
                                                       V  R  t d

                    where:
                            V  L    the fluid v olume
                            V  R    the reactor v olume.
                      So,  r , r , r , and   r are the appropriate rates for expressing the intrinsic catalytic reac-
                             vs
                                      t
                                s
                          m
                    tion rate, whereas   r  u  and   R  are phenomenological rates, used for reactor design. More
                    specifically,  r is also called the “pseudo-homogeneous rate” (Schmidt, 2005).
                               u
                      For these rates, the following is v alid:
                                              1d  N  V      S     M
                                         r            S  r  vs     r    S  r  m        (3.18)
                                                               s
                                          u
                                             V  L  t d  V  L  V  L  V  L
                    v The oerall rate of reaction (  R ) per unit volume of the reactor is (Le 1972) v enspiel,
                                          1d  N   V      S     V     M
                                      R            S  r  vs     r    L  r    S  r  m   (3.19)
                                                            s
                                                                  u
                                          V  R  t d  V  R  V  R  V  R  V  R
                      The design of a reactor is connected to certain preferred parameters and it is useful to know
                    how they are related to each other. For instance, it is v ery important to use the appropriate
                    terms in order to correlate the reactor volume to the fluid and solid v olumes. In  able 3.1,  T
                    the most important ratios per reactor are presented.   V  R  denotes the total volume of the reactor,
                    V  S  denotes the volume of the solid, and   V  L  is the fluid volume in two-phase systems and the
                    liquid-volume in three phase systems.
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