Page 49 - Elements of Chemical Reaction Engineering Ebook
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20                                             Mole  Balances   Chap. 1

                            The feed consists of 3 to 7% HNO,,  59 to 67% H,SO,,  and 28 to 37% water.  Sul-
                            furic acid is necessary to adsorb the water and energy generated by the heat of reac-
                            tion.  The  plant,  which  produces  15,000 lb  nitrobenzenelh,  requires  one  or  two
                            operators per shift together with a plant supervisor and part-time foreman. This exo-
                            thermic reaction  is carried out essentially  adiabatically,  so that the temperature of
                            the feed stream rises from 90°C to 135°C at the exit. One observes that the nitroben-
                            zene stream from the separator is used to heat the benzene feed. However, care must
                            be taken  so that  the temperature  never  exceeds  19O0C, where  secondary reactions
                            could result in an explosion. One of the safety precautions is the installation of relief
                            valves that will rupture before the temperature approaches  1 9O"C, thereby  allowing
                            a boil-off  of water and benzene, which would drop the reactor temperature.

              What are the  Gas-Phase Reactions.  The tubular  reactor  [Le., plug-flow reactor  (PFR)]  is
            advantages and   relatively easy to maintain (no moving parts), and it usually produces the high-
          disadvantages of a
                   pm?   est conversion per  reactor  volume  of  any  of  the  flow reactors.  The disadvan-
                         tage of  the tubular reactor is that it is difficult to control temperature within the
                         reactor, and hot spots can occur when the reaction  is exothermic. The tubular
              CSTR: liquids  reactor is commonly  found either in the form of  one long tube or as one of  a
                PFR: gases
                         number  of  shorter reactors arranged  in  a tube bank  as shown in Figure  1-12.
                         Most  homogeneous  liquid-phase  flow  reactors  are  CSTRs,  whereas  most
                         homogeneous gas-phase flow reactors are tubular.
                              The costs of  PFR  and PBR  (without catalyst)  are similar to the costs of
                         heat  exchangers  and  thus  can  be  found  in  Plant  Design  and  Economics for
                                    n






























                              Figure 1-12  Longitudinal tubular reactor. [Excerpted by special permission from
                              Chern. Eng., 63(10), 21 1 (Oct. 1956). Copyright 1956 by McGraw-Hill, Inc., New
                              York, NY  10020.]
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