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288  13 Key-Study on NHase/AMase System


                      Reaction rate (μmol) (min U NHase ) −1  0.10













                        0.01
                           0          20         40         60         80
                                            Process time (h)

                    Figure 13.1  Effect of acrylonitrile con-  at various concentrations of acrylonitrile:
                    centration on time course of reaction rate  , 100 mM acrylonitrile and 3.6 U  ;
                                                                            NHase
                    of NHase activity in in situ cascade bi-  and with 107 U  and  ,100 mM;  ,
                                                               NHase
                    enzymatic system of M. imperiale resting  300 mM;  , 600 mM;  , 800 mM; Δ,1 M
                                             ◦
                    cells. The runs were performed at 4 C,  acrylonitrile.
                    after 58 h. The semi-log plot of the reaction rate versus time gave a straight line
                    (indicating a first-order deactivation mechanism), whose slope gives the inactivation
                    constant k . The data in Figure 13.1 show that a first-order deactivation mechanism
                            d
                    held for all the conditions examined. As the 100 mM acrylonitrile run with 107
                    U      reached 78% conversion (reactor operated under integral conditions),
                      NHase
                    a second run was performed with a lower enzyme load, 3.6 U  , reaching
                                                                        NHase
                    6% conversion (reactor operated under differential conditions). For the 100 mM
                    substrate run at 107 U  , the inactivation of enzyme was clearly significantly
                                      NHase
                    reduced. Under these conditions, acrylonitrile conversion was rather high during
                    the whole run and varied from 78% to 68% within 24–70 h. The loaded enzyme
                    was in excess and only part of it was involved in the reaction; as soon as a part
                    of the enzyme was inactivated, it was replaced by active molecules. As a result,
                    the apparent inactivation constant (k ) was lower than in the other experiments,
                                                 d
                    and the same was the case for the specific reaction rate. However, the enzymatic
                    activity of resting cells operating in the presence of a relatively high acrylonitrile
                    concentration (200 and 500 mM) underwent a marked decline. At relatively low
                    substrate concentration, the enzyme activity was maintained during the whole
                    process. The inactivation constant appeared to be relatively low at low substrate
                    concentrations; but the higher the substrate concentration in the feed stream,
                    the higher was the rate of activity loss [20]. Similar findings on NHase activity
                    reduction by elevated substrate concentrations have been observed by others.
                    Nagasawa et al. [13] described a reduction of NHase activity when using an
                    acrylonitrile concentration as high as 1.3 M and the need for a fed-batch bioreactor
                    for acrylonitrile bioconversion. Graham et al. [28] also described an inhibition of
                    this enzyme by acrylonitrile concentrations over 200 mM and a complete loss of its
                    activity at 500 mM acrylonitrile.
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