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Else_AIEC-INGLE_cH003.qxd  7/13/2006  1:45 PM  Page 93
                  3.3 T Reactors o-Phase Agitated  w            93


                  where:
                          Q  z    the volumetric flow rate in the reactor at length   z
                          x    the conersion of the limiting reactant at the same length v
                              the expansion f actor .
                           R
                  In f the space-time as defined aboe is the superficial space time, as it is based
                   v
                  ed-beds,
                  ix
                  on the total volume of the bed. The real space-time for a bed of bed v oidage     is
                                                       V
                                                   	    R                           (3.100)
                                                      Q
                                                        i
                  ix Another important feature related to mean residence time in fed-beds is the fluid holdup
                  based on the empty bed v olume   h  e,t  . If the fluid occupies the whole empty bed
                                                                         ,
                  volume, then   h  e,t     . Ho this is not the case when   h  e,t      i.e. when there is a
                                    v
                                   ,
                                    er
                                    we
                  bypass of the fluid from some regions in the bed, most commonly in the upper section of the
                  bed in a downflow operation, and the fluid is a liquid. In this case, the real residence time is
                                                      hV e,t  R
                                                 t                                  (3.101)
                                                  m
                                                       Q
                                                        i
                  The actual residence time of a reactor is measured by employing residence time distrib u-
                  tion (RTD) experiments utilizing tracing techniques. Furthermore, seeral correlation v
                  forms estimating the fluid holdup can be found in the related literature.
                  Space velocity in flow r s eactor
                  The number of reactor volumes of feed at specified conditions, which can be treated in a
                  unit time is called “space v and is (Le 1972) enspiel, v
                  elocity”
                                                    1   Q
                                                 s        i                         (3.102)
                                                    	   V
                                                         R
                  This parameter is frequently used in ion-exchange and adsorption operations in fixed-beds
                  and it is frequently called “relati olumetric flo v e v w rate”:

                                                Q    QV
                                             s    i     rel  R  Q    rel            (3.103)
                                                V     V
                                                 R     R
                  The most common unit of   Q  rel  is bed volumes per hour (BV/h). Space velocity is also used
                  ix in catalytic reactors, especially in three-phase fed-beds, and is referred to as liquid hourly
                  space velocity (LHSV) for the liquid phase, and gas hourly space v elocity (GHSV) for gas
                  phase.  As mentioned abo space-time and space velocity are measured under the
                   e,
                    v
                                  er
                                  ,
                  entrance conditions  . Ho for space v other conditions are frequently used
                                  v
                                    ,
                                    elocity
                                  we
                  (Fogler, 1999). F the LHSV is measured at 60 to 75 °F and GHSV at standard or e xample,  ,
                  temperature and pressure.
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