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T 1
H +
HOO His
H 2 O 2
O 2 - + H +
His Fe 3+
His
OH - /OH 2
k 1
His
Cys
k 2
His
k 2 ´
HO His
H 2 O His
p K a = 6.1
Fe 2+
H +
His
His
Glu
His Fe 3+
His
His Fe 3+
His
His
Cys
His
Cys
H 2 O 2
His
Cys
T 2
Glu
k 3
O C
O
H 2 PO 4 -
His
Glu
Cellular
Reductants
His Fe 3+
His
His
Cys
OH
Glu
Final
p K a = 9.6
O
P
OH
H 2 PO 4 -
O His
T 2P
HO His
His Fe 3+
His
His Fe 3+
His
His
Cys
His
Cys
Figure 4.7. catalytic cycle of superoxide reductase, showing only the observable inter-
mediates. Large arrow: reductive cycle; narrow arrows: oxidative cycle (adapted from
Pinto et al. [115] with the permission of Elsevier Inc.). See color insert.
intermediate, T1, with an absorption maximum at ca. 620 nm, which occurs at
a second-order rate constant of ∼10 9 /M/s (Table 4.4). TI intermediates have
been suggested to be ferric-(hydro)peroxo species, which decay subsequently
to another intermediate, T2, in the case of A. fulgidus . This step is a pseudo-
first-order, unimolecular process (Table 4.4). The optical properties of T2 are
identical to those reported for the basic form of ferric SOR [118]. T2 decays
further to the resting oxidized state through a unimolecular process for the
wild-type enzyme. This resting form was observed for the D. vulgaris enzyme
T1 without the formation of T2. However, both intermediates, T1 and T2, were
observed for the 1Fe-SOR from Treponema pallidum and 2Fe-SOR from
Desulfoarculus baarsii [115]. The nature of intermediates T1 and T2 has been
reviewed in detail [115]. Overall, progress has been made for the last few years
on the elimination of superoxide by 1Fe- and 2Fe-SOR, but several issues still
need to be resolved. These include the number of catalytic intermediates,
reasons of low SOD activity of SOR, although thermodynamic properties
 
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