Page 228 - Fluid mechanics, heat transfer, and mass transfer
P. 228

206   TWO-PHASE FLOW SYSTEMS










































                                         FIGURE 7.12  Typical fluid bed catalytic cracking unit.



                 & The reaction is endothermic and carbonaceous res-  & Seal legs are frequently used in conjunction with
                  idue isdeposited onthe catalyst particles, reducing its  solids flow control valves to equalize pressures and to
                  activity. The catalyst is continuously removed for   strip trapped or adsorbed gases from the solids.
                  regeneration and reheating. It passes down through  & Catalyst is transferred between the reactor and the
                  the reactor stripper in which unconverted hydrocar-  regenerator through standpipes/seal legs and risers.
                  bons are removed and then through a standpipe and  & Seal and/or stripping gas is introduced near the
                  transfer line to the regenerator vessel.
                                                                       bottom of the leg. This gas flows both upward and
                 & In the regenerator, air is used as the fluidizing gas
                                                                       downward. The transfer line is aerated with a high
                  and the coke deposits are burned off the catalyst    gas flow, thereby reducing the density there to a
                  particles. The burning is highly exothermic and      much lower value than that in the standpipe. This
                  provides the heat necessary for the cracking reac-   resulting pressure imbalance causes the desired
                  tion. The hot regenerated catalyst is then returned to  catalyst flow.
                  the reactor.                                       & Bulk density in the standpipe is fairly high and the
                 & Steam is normally used to strip the catalyst particles
                                                                       hydrostatic pressure produced at the bottom is
                  from the interstices of the solids as well as gases  substantial.
                  adsorbed by the particles.
                                                                     & Accurate pressure balances between vessels across
                 & There are a number of variations in the design of   the standpipe/riser loops are essential for proper
                  catalytic cracking and reforming units. Figure 7.13  design of a fluid–solids unit.
                  gives another variation used in fluid catalytic crack-  . What is vibrofluidization?
                  ing units.
                                                                     & When a fluidized bed is given vibrations, the process
               . What is the function of standpipes/seal legs in fluid bed
                                                                       is called vibrofluidization. The bed of solids is
                solids transfer lines?
   223   224   225   226   227   228   229   230   231   232   233