Page 352 - Elements of Chemical Reaction Engineering Ebook
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Chap. 6   Questions and Problems                               323

                                         The feed, which is equimolar in A and C, enters at a flow rate of  10 Ib
                                         mol/s. What reactor volume is required for a 50% conversion of A to B?
                                         (Am: V  = 105 ft3.)
                              P6-5,   A mixture of 50% A, SO% B is charged to a constant-volume batch reactor in
                                      which  equilibrium is rapidly achieved. The initial total  concentration is  3.0
                                      mol/dm3.
                                      (a)  Calculate the equilibrium concentrations and conversion of  A  at  330  K
                                         for the reaction sequence

                                     Reaction 1:  A + B e C 4 D  K,,  (330 K) = 4.0,   K,,  (350 K) = 2,.63.
                                                             +
                                                           X
                                                              Y
                                     Reaction 2:  C + B e K,,(330  K) = 1.0,      KC2 (350 K) = 1.51
                                      (b)  Suppose now the temperature is increased to 350 K. As a result, a third
                                         reaction must now be considered in addition to the reactions above:
                                            Reaction 3: A + X e Z     K,,  (350 K) = 5.0 dm3/mol
                                         Calculate  the_ equilibrium  concentrations, conversion  of  A  and  overall
                                         selectivities SCX , SDZ , and  SYZ .
                                      (c)  Vary the temperature-over the-range  300 to  500  K  to  learn  the  effect
                                         of  selectivities SCX , SDZ, and Syz  on temperature.
                                         Additional information:
                                               AH,,  = -20,000 Jlmoi A   AHRz = +20,000 Jlmol B
                                                         AH,,  = -40,000 J/mol A
                               P6-6*   Consider the following system of gas-phase reactions:
                                              A  __j X  rx = k,       k, = 0.002 rnoYdm3.min
                                                       B
                                              A  +  rB = kzCA  k, = 0.06 min-1
                                               A  ---+   I'   ry = k3Ci   k, = 0.3 dm3/mol * min
                                      B is the desired product, and X and Y are foul pollutants that are expensive: to
                                      get rid of. The specific reaction rates are at 27°C. The reaction system is to be
                                      operated at 27°C and 4 atm. Pure A enters the system at a volumetric flow rate
                                      of  10 dm3/min.
                                      (a)  Sketch the instantaneous selectivities (S,,,  SB,,and S,,,   = rB/(rx + rll))
                                          as a function of the concentration of CA.
                                      (b)  Consider a series of reactors. What should be the volume of the first reactor?
                                      (c)  What are the effluent concentrations of A, B, X, and Y from the first reactor.
                                      (d)  What is the conversion of A in the first reactor?
                                      (e)  If  90'% conversion  of  A  is  desired, what  reaction  scheme  and  reactor
                                          sizes should you use?
                                      (f)  Suppose that El  = 10,000 cal/mol, E2 = 20,000 cal/mol, and E,  = 30,000
                                          cal/mol. What temperature would you recommend for a single CSTR with
                                          a space-time of  10 min and an entering concentration of A of 0.1 mol/dn13?
                               P6-78   Pharmacokinetics concerns the ingestion, distribution, reaction, and elimina-
                                      tion reaction of drugs in the body. Consider the application of pharmacokinet-
                                      ics to one of the major problems we have in the United States, drinking and
                                      driving. Here we  shall model how  long one must wait to drive after having a
                                      tall martini. In most states the legal intoxication limit is  1.0 g of  ethanol per
                                      liter of body fluid. (In Sweden it is 0.5 g/L, and in Eastern Europe and Russia
                                      it is any value above 0.0 g/L.) The ingestion of  ethanol into the bloodstream
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