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542                     Unsteady-State Nonisothermal Reactor Design   Chap. 9

                            Example 9-2  Safety in Chemical Plants with Exothermic Reactions
                            A  serious accident  occurred  at  Monsanto plant  in  Sauget, Illinois,  on August  8 at
                             12:18  A.M.  (see  Figure  E9-2.1).  The  blast  was  heard  as  far  as  IO miles  away  in
                            Belleville,  Illinois,  where  people  were  awakened from their  sleep.  The  explosion
                            occurred in a batch reactor that was used to produce nitroandine from ammonia and
                            o-nitrochlorobenzene  (ONCB):




































            Was a Potential
           Problem Analysis    Figure E9-2.1 Aftermath of the explosion. (St. Louis Globe Democrat photo by
               carried out?    Roy  Cook  Courte5y of St. Louis Mercantile Library.)
                            This reaction  is normally  carried out isothermally  at  175°C and about 500 psi. The
                            ambient temperature of the cooling water in the heat exchanger IS 25°C. By adjusting
                            the coolant rate the reactor temperature could be maintained at  175°C. At the maxi-
                            mum coolant rate the ambient  temperature 15 25°C throughout the heat  exchange.
                                On the day of the accident, two changes in normal  operation  occurred.
                              1.  The reactor  was charged  with  9.044 kmol  of ONCB, 33.0 kmol of  NH3, and
                                 103.7 kmol  of  H20. Normally,  the  reactor  15  charged  with  3117  kmol  of
                                ONCB,  103.6 kmol of H20, and 43 kino1 of NH3.

                           Adapted  from  the  problem  by  Ronald  Willey,  Seminar  on  a  Nirroanaline  Reactor
                          Rupture.  Prepared  for SACHE, Center for Chemical Process  Safety, American  Insti-
                          tute of Chemical Engineers, New York (1994). The values of AH,,  and UA were esti-
                          mated  in  the  plant  data  of  the  temperature-time  trajectory  in  the  article  by  G. C.
                          Vincent, Loss Prevention, Vol. 5. p. 46-52, AIChE, New York  NY.
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