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5.7 Problems for Chapter 5 109

                                                           (i) A + B + C
                                                         or (ii) A -+ B,
               v
                                                             A-+C
            “OF
                                                                  B + C
                                                        or (iii) A +
           0                5-2 Suppose the reaction in Example 5-4 was studied in a CSTR operated at steady-state, and the

                               results given below were obtained. Calculate the values of  kf  and  k,,  and hence write the rate
                               law. Assume  T  to be the same, constant density, and no D in the feed.


                                                 flh         1    2    3    4
                                                 100  CAIC~~  76.5 65.9 57.9 53.3
           0                5-3 The liquid-phase hydrolysis of methyl acetate (A) to acetic acid and methyl alcohol is a re-
               V
            “O-T
                               versible reaction (with rate constants  kf  and  k,,  as in equation 5.3-3). Results of an experiment
                               carried out at a particular (constant) temperature in a BR in terms of the fraction hydrolyzed
                               (f~)  measured at various times (t), with  CA0  = 0.05 mol  L-t  (no products present initially),
                               are as follows (Coulson et al., 1982, p. 616):


                                              tls  0   1350  3060  5340  7740   00
                                              f*  0   0.21  0.43  0.60  0.73  0.90


                               (a) Write the chemical equation representing the reaction.
                               (b) Obtain a rate law for this reaction, including values of the rate constants. State any as-
                                   sumption(s)  made.
                            5-4 In an experiment (Williams, 1996) to evaluate a catalyst for the selective oxidation of propene
                               (CsH6)  to various products, 1 g of catalyst was placed in a plug-flow reactor operated at 450°C
                               and 1 bar. The feed consisted of propene and air (21 mole %  02,79%   NZ  (inert)). GC analysis
                               of the inlet and outlet gas gave the following results, the outlet being on a water-free basis
                               (Hz0  is formed in the oxidation):


                                        Substance             Inlet mole %   Outlet mole %
                                                                  10.0            ?
                                        propene  (C3H6)
                                                                  18.9            ?
                                        oxygen (02)
                                        nitrogen  (N2,  inert)    71.1           78.3
                                        acrolein  (C3H40)          0             3.17
                                        propene oxide  (CsHsO)     0             0.40
                                        acetaldehyde  (CzH40)      0             0.59
                                        carbon  dioxide            0             7.91

                                (a) If the feed rate of C3H6 is FQQ~ = 1  mm01  min-‘,  at what rate do (i) CsH6.  (ii) 02,  and
                                   (iii)  Hz0  leave the reactor?
                               (b) What is  j&,  the fractional conversion of  CsHh?
                                (c) What is the selectivity or fractional yield of each of acrolein, propene oxide, and  acetalde-
                                   hyde with respect to propene?
                               (d) What is the rate of reaction expressed as (i) (-TQQ);  (ii) rc,n,o (in mm01 min-’ (g
                                   cat)-‘)?  Assume that the reactor acts as a differential reactor (Section 3.4.1.3.1).
                            5-5 Repeat Example 5-6 for a CSTR with V = 15 L and 4 = 1.5 L  min-‘.
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