A.N. Biswas et al. / Journal of Molecular Catalysis A: Chemical 326 (2010) 94–98
97
is obtained; while the dA/dt0 vs. [F15TPCFe(IV)Cl] plot gives a value
of 1.01 × 103 dm3 mol−1. In the latter case the lower value of the
second order rate constant suggests greater catalyst decomposition
at high catalyst concentration.
4. Conclusion
A significantly high catalytic activity of the iron(IV)corrole com-
plex in the oxidation of alkanes at room temperature with m-CPBA
has been achieved. For the first time in metallocorrole chemistry,
cyclohexane has been hydroxylated with 100% selectivity produc-
ing cyclohexanol in 50% yield. This is also the first report of the
hydroxylation of adamantane catalyzed by any metallocorrole. The
overall conversion in the hydroxylation of adamantane is achieved
up to 75% with 3◦/2◦ ratio of 10.3–10.7. To the best of our knowledge
these are the highest yield conversions of C–H bonds to C–OH bonds
in metallocorrole chemistry, where the carbon is sp3 hybridized.
The kinetic investigation reveals a first order reaction rate depen-
dence on the concentration of catalyst as well as on that of the
oxidant.
Fig. 3. Plot of (dA/dt)0 vs. [m-CPBA].
Acknowledgement
The financial support (SR/S1/IC-08/2007) from DST, Govern-
ment of India, is gratefully acknowledged.
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Scheme 1. Metalloporphyrin-catalyzed oxidation.
Figs. 3 and 4 respectively. It is clear that the data are best fitted by
a first order dependence of dA/dt0 on the concentration of m-CPBA
as well as on the concentration of catalyst F15TPCFe(IV)Cl.
Since substrate has always been taken in excess, the dependence
of dA/dt0 on substrate concentration has been ignored and overall
dA
dt
(1)
The relation (1) is compatible to the generally accepted mecha-
nism of metalloporphyrin-catalyzed oxidation shown in Scheme 1
[6], which involves slow rate-determining conversion of the cat-
alyst to an oxidized intermediate, which then transfers oxygen to
the substrate in a fast step. Here the absorbance vs. time plot (Fig. 2)
is clearly biphasic in nature having a hyperbolic component (slow
process) followed by an exponential component (fast process).
From the slope of the dA/dt0 vs. [m-CPBA] at constant [F15
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TPCFe(IV)Cl], second order rate constant k1 (1.21 × 104 dm3 mol−1
)