C O MMU N I C A T I O N S
Figure 2. Dependence of the stabilized rate (symbols: measured, solid
line: calculated) on [S4O6 ]0. [ClO2 ]0 ) 0.04822 M, pH ) 4.95. All
other initial concentrations are zero in the simulation.
Figure 4. Calculated rates of eqs 1-5 at t ) 100 s plotted against initial
tetrathionate concentration. [ClO -] ) 0.04822 M, pH ) 4.95.
2
-
-
2
0
but that the autocatalytic pathway quickly comes to dominate as
2
-
[S
4
O
6
] is increased, resulting in the rapid rise in the rate seen in
2-
2-
Figure 2 for pS
the HSO
4
O
6
around 3. As we continue to increase S
4
O
6
,
-
3
produced in steps 1 and 4 begins to capture a significant
amount of the autocatalyst in step 5, which overtakes step 4 at about
2-
pS
behavior as [S
order with respect to S
4
O
6
) 2.7 (Figure 4), causing the rate to show saturation
2-
O
4 6
] is increased further. The high formal kinetic
2-
O
4 6
arises from the turning on and turning
off of the autocatalytic pathway as we sweep through a range of
initial tetrathionate concentrations.
We emphasize that only the formation of chlorine dioxide, not
the disappearance of tetrathionate and chlorite ion, becomes
2-
independent of [S
O
4 6
0
] . It should also be noted that the net rate
of chlorine dioxide formation may start to decrease at higher
tetrathionate concentrations because of the increasing importance
of the chlorine dioxide-tetrathionate reaction.9
Investigations are continuing in our laboratory to extend this
mechanism so as to describe accurately the kinetics and mechanism
of the chlorite-tetrathionate reaction over its entire time course.
Figure 3. Calculated rates of eqs 1-5 at t ) 100 s plotted against initial
2
-
chlorite concentration. [S4O6 ]0 ) 0.0005 M, pH ) 4.95.
-
6
) (1.0 ( 0.2) × 10 M s-1 and k
5
-1
1
(
.3) × 10 M-1 s-1, k
2
4
) 98
7 M s-1, were determined by nonlinear parameter estimation
-
1
1
6
with the multipurpose kinetic program package ZiTa. The two
data series (chlorite- and tetrathionate-dependence) were fitted
separately. The value obtained for k
found at very different pH and ionic strength in a study of the
4
is within a factor of 3 of that
Acknowledgment. This work was supported by Grant CHE-
0306262 from the U.S. National Science Foundation and OTKA
Grants T30446 and T029838 from the Hungarian Research Fund
as well as by the U.S.-Hungarian cooperative program. A.K.H is
grateful for the financial support of OTKA postdoctoral fellowship
Grant D38001.
7
2-
reaction of HOCl and S
1
4
O
6
2
. Our k differs by about a factor of
5 from that obtained in a study17 done in a large excess of sulfite
rather than chlorite. The calculated and measured rates are in
excellent agreement, as seen in Figures 1 and 2.
The unusual kinetic behavior of this system can be understood
by referring to eqs 1-5. The key species is the autocatalyst Y
References
(
HOCl). To analyze the chlorite dependence, we focus on the
(1) Orb a´ n, M.; Epstein, I. R. J. Phys. Chem. 1982, 86, 3907.
(
(
(
2) Orb a´ n, M.; De Kepper, P.; Epstein, I. R. J. Phys. Chem. 1982, 86, 431.
3) Nagyp a´ l, I.; Epstein, I. R. J. Phys. Chem. 1986, 90, 6285.
4) Nagyp a´ l, I.; Bazsa, Gy.; Epstein, I. R. J. Am. Chem. Soc. 1986, 108, 3635.
competition between the nonautocatalytic and autocatalytic path-
ways 1 and 4. At low [ClO
and its rate increases with [ClO
net production of HOCl at a rate proportional to [ClO
these two rates cross (see Figure 3) at about pClO
(
ClO
at pClO
shut down. Now the reaction is dominated by the nonautocatlytic
production step 1, and the net rate begins to increase with [ClO
The apparent selfinhibition in the range 1.85 < pClO
from the switching between the relatively rapid autocatalytic route
to the slower nonautocatalytic pathway. Note that ClO
sense, to buffer [HOCl], since, at low [HOCl], production of HOCl
and removal of HSO
relative to step 3 and prevent step 5 from becoming a significant
sink for HOCl.
-
2
], autocatalysis is the favored route,
-
], because r
2
> r
3
, resulting in
(5) Peintler, G.; Nagyp a´ l, I.; Epstein, I. R. J. Phys. Chem. 1990, 94, 2954.
(6) Horv a´ th, A. K.; Nagyp a´ l, I. J. Phys. Chem. A 1998, 102, 7267.
2
-
2
-
]. After
(
7) Horv a´ th, A. K.; Nagyp a´ l, I. Int. J. Chem. Kinet. 2000, 32, 395.
(8) Csord a´ s, V.; Bubnis, B.; F a´ bi a´ n, I.; Gordon, G. Inorg. Chem. 2001, 40,
833.
9) Horv a´ th, A. K.; Nagyp a´ l, I.; Epstein, I. R. J. Phys. Chem. A 2003, 107,
0063.
2
) 1.85
1
maximum in Figure 1), autocatalysis becomes less important as
(
-
2
increases. Once the rate of step 4 falls below that of step 1,
1
-
≈ 1.3 (minimum in Figure 1), autocatalysis is essentially
(10) Horv a´ th, D.; T o´ th, AÄ . J. Chem. Phys. 1998, 108, 1447.
2
(
(
11) T o´ th, A.; Lagzi, I.; Horv a´ th, D. J. Phys. Chem. 1996, 100, 14837.
12) Horv a´ th, D.; Kiricsi, M.; T o´ th, AÄ . J. Chem. Soc., Faraday Trans. 1998,
94, 1217.
-
2
].
-
(13) Horv a´ th, A. K.; Nagyp a´ l, I.; Epstein, I. R. J. Am. Chem. Soc. 2002, 124,
0956.
14) Gordon, G.; Tachiyashiki, S. EnViron. Sci. Technol. 1991, 25, 468.
(15) Fogelman, K. D.; Walker, D. M.; Margerum, D. W. Inorg. Chem. 1989,
8, 986.
2
< 1.3 results
1
(
-
2
acts, in a
2
(
16) Peintler, G. ZiTa, version 5.0; A Comprehensive Program Package for
Fitting Parameters of Chemical Reaction Mechanism; J o´ zsef Attila
Tudom a´ nyegyetem: Szeged, Hungary, 1989-1998.
-
3
in step 2 assume increased importance
(
17) Huff Hartz, K. E.; Nicoson, J. S.; Wang, L.; Margerum, D. W. Inorg.
8 2
Chem. 2003, 42, 78. The value obtained there for k (k ), after adjustment
to pH 4.95, is 6300 M-
JA048982L
1
s
-1
.
When the initial tetrathionate concentration is varied as in Figures
2-
2
4 6
and 4, we find that steps 1 and 4 have similar rates at low [S O ]
J. AM. CHEM. SOC.
9
VOL. 126, NO. 20, 2004 6247