Page 449 - Elements of Chemical Reaction Engineering Ebook
P. 449

Nonelementary Reaction Kinetics   Chap. 7

                                  Run 1:
                                  rime (h)          0   10   15   20   30   40   50   60   70
                                                  I
                                  Cell Density    /  2.7   2.8  15   70   400   600  775  600  525
                                   (cells/mL) X



                                  Run 2:
                                  Time (h)         0    5   10   15   20   30   40   50   60
                                  Cell density     2.7   7   11   80   250  350   350  250   -
                                   (~elIs11nL) X  lob4

                                  % H2S            0.1   0.7   0.7   0.8   1.2   4.3   7.5  11.0  12.3

                                  (a)  What is the lag time with and without the yeast extract?
                                 (b)  What is the difference in the specific growth rates, kmax, of  the bacteria
                                     with and without the yeast extract?
                                 (c)  How long is the stationary phase?
                                 (d)  During which phase does the majority production of  H2S occur?
                                 (e)  The liquid reactor volume in which these batch experiments were carried
                                     out was 0.2 dm3. If this reactor were converted to a continuous-flow reac-
                                     tor, what would be the corresponding wash-out rate?
                          W-2&  Cell  growth  with  uncompetitive  substrate  inhibition  is  taking  place  in  a
                                 CSTR. The cell growth rate law for this system is





                                 with  kmax =  1.5 h-l,  Ks =  1 g/dm3, KI = 50 g/dm3, Cd =  30  g/dm3,
                                 Y,,, = 0.08, Cd = 0.5 g/dm3, and D = 0.75 h-l.
                                 (a)  Make a plot of the steady-state cell concentration C, as a function of D.
                                 (b)  Make a plot of  the substrate concentration Cs as a function of D on the
                                     same graph as that used for part (a).
                                 (c)  Initially, 0.5 g/dm3 of bacteria was placed in the tank containing the sub-
                                     strate and the flow to the tank started. Plot the concentrations of bacteria
                                     and substrate as functions of  time.
                          W-27B  A solution containing bacteria at a concentration of 0.001 g/dm3 was fed to a
                                 semibatch reactor. The nutrient was in excess and the growth rate law is first
                                 order  in  the  cell  concentration.  The  reactor  was  empty  at  the  start  of  the
                                 experiment. If the concentration of bacteria in the reactor at the end of 2 h is
                                 0.025 g/dm3, what is the specific growth rate k in min-I?
                          W-28* An understanding of bacteria transport in porous media is vital to the efficient
                                 operation of the water flooding of petroleum reservoirs. Bacteria can have both
                                 beneficial  and  harmful  effects on  the  reservoir.  In  enhanced  microbial  oil
                                 recovery, EMOR, bacteria are injected to secrete surfactants to reduce the inter-
                                 facial tension at the oil-water  interface so that the oil will flow out more easily.
                                 However, under some circumstances the bacteria can be harmful, by plugging
                                 the pore space and thereby block the flow of water and oil. One bacteria that
                                 has been  studied, Leuconostoc mesenteroides, has the unusual behavior that
                                 when  it  is  injected  into  a  porous  medium  and  fed  sucrose,  it  greatly
   444   445   446   447   448   449   450   451   452   453   454