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290  13 Key-Study on NHase/AMase System

                       300      First CSMR        Second CSMR      120

                       250                          Slope = 0.618  100
                      3-Cyanopyridine (mM)  150  Slope = 0.535     60   Total product formed (mmol)
                       200
                                                                   80


                       100
                                                                   40
                        50                          Slope = 0.379  20
                                   Slope = 0.066
                         0                                         0
                          0   25  50  75  0   25  50  75 100 125 150
                                         Process time (h)

                    Figure 13.3  Comparison of the perfor-  loaded with 4000 U NHase  and 480 U AMase ). In
                    mances of two bioreactors working in series.  the first CSMR, 3-cyanopyridine (Δ) was con-
                    The feed of the first CSMR is a solution  verted at steady state up to 50%; the total
                    of 300 mM 3-cyanopyridine (in 50 mM Na-  conversion occurred in the second CSMR
                    phosphate buffer, pH 7.0); the outflow of  (▴). The total acid and nicotinamide formed
                    the first reactor was fed to the second one.  refer to the right-hand axis and are indicated
                    These bioreactors were operated under the  as  ,  and  ,  respectively.
                                  ◦
                    same conditions (5 C, 250 rpm, 3 ml h −1  and
                    the AMase-catalyzed reaction occurring in the second CSMR was markedly higher
                    than the one in the first CSMR (Figure 13.3) [26], as indicated by the ratio of the
                    slope of the data at steadystate (0.379/0.066). In Figure 13.3, P tot  is calculated at
                    each time of collection according to the formula where V and P are, respectively,
                                                                 i
                                                                      i
                    the volume and the product concentration of the ith fraction, and k labels the
                    current fraction.
                               k
                              ∑
                         P tot  =  V [P] + V [P] k
                                     i
                                  i
                                        R
                              i=1
                      This was assumed to be caused by the almost zero concentration of 3-
                    cyanopyridine in the second CSMR compared to the first one (150 mM at
                    steadystate regime). These results motivated the investigation on the effect of
                    high 3-cyanopyridine concentrations on the AMase reaction rate. The possibility of
                    inhibiting and/or inactivating the AMase by an appropriate nitrile concentration
                    in the feed stream would help to stop the process at the amide stage even when
                    using whole cells. To this end, long-term experiments were performed in a CSMR
                                                                        −1
                    fed with 100 mM nicotinamide for 53 h, at a flow rate of 12 ml h ,thisprocess
                    time being sufficient to totally inactivate the NHase activity. The reactor was then
                    fed with a buffered solution containing both 100 mM nicotinamide and various
                                                                       ◦
                    concentrations of 3-cnp [33]. The reactor was loaded with 24 U 20 C  (=200 mg of
                                                                      AMase
                                      ◦
                    resting cells), kept at 50 C, and stirred (250 rpm). In the absence of 3-cyanopyridine
                    in the feed, the k -value of AMase was negligible. The inactivation constants calcu-
                                 d
                    lated once the bioreactors reached steadystate conditions are shown in Figure 13.4.
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