Page 132 - Introduction to chemical reaction engineering and kinetics
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114  Chapter 5: Complex Systems

                                a catalyst of  VzOs   -  Moos  on silica gel. In a series of experiments, they varied the space time
                                r = W/F,  where  W  is the weight of catalyst and  F  is the total molar flow rate of gas (T  in (g
                                cat) h  mol-‘),  and analyzed for M and  CO2  (C) in the outlet stream. (W/F  is analogous to the
                                space time  V/q,  in equation 2.3-2.) For one series at 350°C and an inlet ratio  (FJFB),  = 140,
                                they reported the following results, with partial pressure  p  in atm:


                                         r  = WIF    l@PB      103PM    102Pc     102PH,0
                                            0         1.83      0         0         0
                                           61         1.60     1.36      0.87      0.57
                                           99         1.49     1.87      1.30      0.84
                                           131        1.42     2.20      1.58      1.01
                                           173        1.34     2.71      1.82      1.18
                                           199        1.32     2.86      1.93      1.25
                                           230        1.30     3.10      1.97      1.30
                                           313        1.23     3.48      2.24      1.47


                                In the following, state any assumptions made and comment on their validity.
                                (a) Since there are six species involved, determine, from a stoichiometric analysis, how many
                                   of the partial pressures  (pi)  are independent for given (T, P), that is, the smallest number
                                   from which all the others may be calculated. Confirm  by:alculation  for  W/F =  313.
                                (b) For W/F = 313, calculate (i) fa; (ii) Ym and Ycm; (iii) Sm and Sc,n.
                                (c) From the data in the table, determine whether  CdHz03(M)  and  CO2  are primary or sec-
                                   ondary  products.
                                (d) From the data given and results above, construct a reaction network, together with corre-
                                   sponding rate laws, and determine values of the rate constants.
                                (e)  The authors used a three-step reaction network to represent all their experimental data
                                   (only partial results are given above):


                                         c&j(B) +  402  -+ QH20s(M)  +  2Coz + 2H20; rl =  klpB

                                                CJH203  + 302 + 4CO2  + H20; I.2 =  k2p~

                                                C.5H6   +  go2   +  6CO2   +  3H@;rs  =  k3pB

                                   Values of  the  rate constants at 350°C reported are: ki  = 1.141 X  10m3;  k2  = 2.468 X  10m3;
                                    ks  = 0.396 X  10m3 mol  h-’ (g cat)-‘.
                                     (i)  Obtain expressions for  pa  and  PM  as functions of  T.
                                    (ii)  Calculate the five quantities in (b) and compare the two sets of results.
                                   (iii)  Does this kinetics model predict a maximum in M? If so, calculate values of  T,,,~~
                                       and  pM,max  .
                                    (iv)  Are there features of this kinetics model that are not reflected in the (partial) data
                                       given in the table above? (Compare with results from (c) and (d).)
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