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444                       Steady-State Nonisothermal  Reactor Design   'Chap. 8

                           and used to design CSTRs (i.e., to obtain the reactor volume or operating tem-
                           perature). If  necessary, the CSTR is either heated or cooled by  a heating or
                           cooling jacket as shown in Figure 8-2, or by  a coil placed inside the reactor.
                                Reactions are frequently carried out adiabatically, often with  heating or
                           cooling  provided  upstream  or  downstream of  the  reaction  vessel.  With  the
                           exception of  processes involving highly viscous materials such as in Problem
                           P8-4, the work done by the stirrer can usually be neglected. After substituting
                           Equation (8-42) for  Q , the energy balance can be written as


             CSTR with heat
                  exchange


                           Under conditions of  adiabatic operation and negligible stimng work, both  Q
                           and wS are zero, and the energy balance becomes


           Adiabatic operation
                 of a CSTR

                               The procedure for nonisothermal reactor design can be illustrated by con-
                          sidering the first-order irreversible liquid-phase reaction shown in Table 8-1.
                          The algorithm for working through either case A or B is summarized in Figure
                          8-4. Its application is illustrated in the following example.
                               From here on, for the sake of  brevity we will let






                          unless otherwise specified.


                          I   Example 8-4  Production of  Propylene Glycol in an Adiabatic CSTR
                          I   Propylene glycol is produced by the hydrolysis of propylene oxide:


                                         CH2-CH-CH3   + H20       CH    CH-CH3
                                         \/                        I  I-1
                                           0                      OH    OH
                            Over 800 million pounds of propylene glycol were produced in  1997 and the selling
            Production, uses,   price was approximately $0.67 per pound. Propylene glycol makes up about 25% of
             and economics   the major derivatives of  propylene oxide. The reaction takes place readily  at room
                            temperature when catalyzed by  sulfuric acid.
                                 You  are the engineer in  charge  of  an  adiabatic CSTR  producing propylene
                            glycol by this method. Unfortunately, the reactor is beginning to leak, and you must
                            replace it. (You told your boss several times that sulfuric acid was corrosive and that
                            mild steel was a poor material for construction.) There is a nice overflow CSTR of
                            33-gal capacity standing idle; it is glass-lined and you would like to use it.
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