V
−
=
of the precursor oxidants (ROOH) to form [(edta)Ru ( O)]
as the reactive oxidizing species in solution. Based on the pKa
values of the ROOH oxidants, the basicity of the ROOH species
is expected to follow the order HSO5− < H2O2 < tBuOOH, which
should also be reflected in the equilibrium constant K for the
formation of the [(edta)RuIII(OOR)]2−/3− intermediates. However,
according to the experimental observations, K is much larger for
t
H2O2 and KHSO5 than for BuOOH, which indicates that the
basicity of the ROOH species seems to be less important than
the steric hindrance caused by the tert-butyl group attached to
the hydroperoxide fragment. On the other hand, the formation
V
−
III
2−/3−
=
of [(edta)Ru ( O)] from [(edta)Ru (OOR)]
will depend on
the ability of this complex to undergo heterolytic cleavage of
the O–O bond expressed by the rate constant k, which in turn
should correlate with the reduction potential of the different
hydroperoxides under consideration, i.e. tBuOOH (E◦ = 1.15 V)17
ꢃ H2O2 (E◦ = 1.78 V) ≤ HSO5 (E◦ = 1.82 V).13 From a
−
Fig. 6 Plots of kꢀobs vs. [POH] for oxidation of ABTS (1 × 10−3 M) by
POH (= KHSO5 (A) and tBuOOH (B)) catalyzed by [Ru(edta)H2O]− (1.0 ×
10−4 M) at 25 ◦C and pH = 6.0 (0.2 M acetate buffer).
combination of the separate trends expected for k and K, and
a comparison of the trend observed in the values of kK at 25 ◦C, it
follows that in addition to the electronic factors considered here,
for which the observed rate constant (kꢀobs) for product formation
should be independent of the substrate concentration. The values
of kꢀ and Kꢀ calculated from the intercept and slope of the plot of
1/kꢀobs versus 1/[KHSO5] are 0.034 0.001 s−1 and 193 6 M−1
at 25 ◦C, respectively. These values are in very close agreement
with the values of k1 (0.031 0.004 s−1 at 25 ◦C) and K1 (227
44 M−1 at 25 ◦C) obtained independently for the reaction of
1 with KHSO5 (see Table 1). These results further substantiate
the validity of the mechanism proposed in Scheme 1. In the
t
−
steric hindrance on BuOOH and HSO5 as compared to H2O2
should further account for the fact that kK is significantly smaller
for tBuOOH and HSO5 as compared to H2O2.
−
Conclusion
In this work a detailed kinetic and mechanistic study of the
reaction between RuIII(edta)(H2O)]− with two hydroperoxides,
tBuOOH and KHSO5, is presented. The findings of this work taken
together with those for the reaction of [RuIII(edta)(H2O)]− with
H2O2,7 strongly suggest that the oxo-transfer from the precursor
oxidant ROOH (H2O2, tBuOOH and KHSO5) to 1 that results in
t
case of BuOOH, non-observance of limiting kꢀobs values at high
[tBuOOH] (Fig. 6B) is typical for the small value of Kꢀ, such
that the observed rate constant (kꢀobs) for oxidation of ABTS to
ABTS•+ does not reach a limiting value at higher [tBuOOH] over
the concentration range studied. The rate-law for the catalytic
oxidation of ABTS in eqn (11) was derived on the basis of the
V
−
=
the formation of the catalytically active [(edta)Ru ( O)] species
should proceed through the formation of [(edta)RuIII(OOR)]2−/3−
t
intermediates (R = H, Bu and SO3−) in a rapid pre-equilibrium
suggested pre-equilibrium and the rate-determining step involving
step, which subsequently undergoes rate-controlling heterolytic
−
the formation of [(edta)RuV O] , can now be simplified to eqn
(13) under such conditions.
=
V
−
=
cleavage of the O–O bond to produce [(edta)Ru ( O)] as a major
product (80–90%). However, in the case of [(edta)RuIII(OOH)]2−
formed in the reaction of 1 with H2O2, the subsequent reaction
kꢀobs = kꢀKꢀ[tBuOOH]
(13)
involves both parallel heterolytic and homolytic cleavage to
The◦close resemblance of the value of kꢀKꢀ (1.52 0.04 M−1 s−1
at 25 C) calculated from the slope of the plot of kꢀobs versus
[tBuOOH] (Fig. 6B) with the value (1.45 0.06 M−1 s−1 at 25 ◦C)
obtained directly (see ESI,† Fig. S3), substantiates the mechanistic
−
produce [(edta)RuV O] and [(edta)RuIV(OH)]− in the ratio of
=
approximately 1 : 1.7 Thus, the tBu and SO3 substituents in
−
[(edta)RuIII(OOR)]2−/3− cause the O–O bond cleavage to clearly
favour heterolysis above homolysis. In this way, the three hydroper-
oxide systems studied so far demonstrate the capability to tune
the fundamental nature of the O–O bond cleavage process, and
underline the advantage of studying such systems in such detail as
reported in this paper.
hypothesis in Scheme 2 for the reaction of 1 with tBuOOH.
−
Since [(edta)RuV O] was obtained as predominant product
=
t
in the reaction of 1 with the precursor oxidants BuOOH and
KHSO5, the common suggested mechanism involves heterolytic
cleavage of the O–O bond. The overall second-order rate constants,
expressed as kK, i.e. the product of the equilibrium constant K
t
for the formation of [(edta)RuIII(OOR)]2−/3− (R = H, Bu and
Acknowledgements
SO3−) and the rate constant k for the subsequent heterolytic
V
−
=
cleavage of the O–O bond to form [(edta)Ru ( O)] , have the
values 26.5
7.0
The authors gratefully acknowledge financial support from the
Deutsche Forschungsgemeinschaft and DST-DAAD (Grant No.
INT/DAAD/P-130/2005). This work is further supported by a
research grant No. SR/S5/BC-15/2006 from the Department of
Science and Technology, Government of India. DC is thankful to
Dr G. P. Sinha, Director of the Central Mechanical Engineering
Research Institute, for support of this work.
t
0.4 (for H2O2),7 1.45
0.06 (for BuOOH) and
2.3 M−1 s−1 (for KHSO5) at 25 ◦C. Since the overall
reaction is a two step process as outlined in Schemes 1 and
t
2, the ability to form [(edta)RuIII(OOR)]2−/3− (R = H, Bu and
SO3−) in the first reaction step through ligand substitution of
[(edta)RuIII(H2O)]− by ROOH, will partially govern the efficiency
This journal is
The Royal Society of Chemistry 2008
Dalton Trans., 2008, 3851–3856 | 3855
©