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Figure 1 shows the kinetics of
alkaline phosphatase activity of the holo-enzyme with different quantities
of alkaline phosphatase. Linear kinetics was observed during the
initial portion of the reaction which exhibited high r2 values by linear
regression (Figure 2). The values were used to generate a linear
standard curve (y = 0.0068x + 0.0661 r2 = 0.994) that correlated enzymatic
activity (dA/dt) with concentration or mass of alkaline phosphatase (Figure
3). The incubation of alkaline phosphatase with Chelex 100 resin
caused a marked change in the absorbance characteristics of the holo-protein
as determined by diode array spectroscopy (Figure 4). These changes
can be clearly observed in Figure 5 which provides an overlay of alkaline
phosphatase (trace in blue) and the apo-protein (trace in red) at 254nm.
Data obtained from the elemental
analysis of the profiles shown in Figure 6 by coupled ICPMS showed the
presence of Zn primarily in peaks eluting at 10.733 and 15.5 minutes.
These peaks occurred in both the holo and the apo enzyme (Figure 7 and
8) respectively. No major signals for Zn were obtained from any of
the other peaks. Enzymatic assays of fractions collected from the
two peaks indicated that activity was present only in the peak eluting
at 10.733 minutes which concurred with the apparent molecular weight of
the enzyme of 150 kDa. Comparisons of the enzyme activity of the
protein normalized samples for this peak gave values of 0.2059 activity/ug
and 0.0548 activity/ug for the holo and apo enzyme respectively.
These values corresponded to a 73% reduction in activity. Quantification
of the zinc associated with the active peak by FIA gave values of 2.779
ng of Zn/ug protein for alkaline phosphatase and 0.718 ng of Zn/ug protein
for apo-alkaline phosphatase indicating a 75% loss of metal which corresponded
closely to the observed decrease in enzymatic activity.
It is concluded that Chelex
100 incubation can sequester Zn from alkaline phosphatase in a manner that
is directly proportional to the observed loss in biological activity.
However, further refinement of the chelation process is required to increase
Zn removal if this procedure is to be used for apo-substrate generation.
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