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M.I. Awad et al. / Inorganica Chimica Acta 344 (2003) 253ꢃ256
/
(NH4)6Mo7O24×
/
4H2O ( abbreviated as Mo(VI)) was
to be first order with respect to PAA, then Eq. (3) can be
integrated to:
purchased from Kanto Chemicals Co., Inc., Japan.
Different concentrations of Mo(VI) solutions were
prepared by dissolving the proper weight in Milli-Q
water.
lnf[PAA]o=[PAA]tgꢀk?t
(4)
where [PAA]t represents the concentration of PAA at
time t. The above equation shows that a plot of
ln{[PAA]o/[PAA]t} versus t would be linear if the
reaction is first order with respect to PAA. The slope
of the straight line is the pseudo-first-order rate constant
of the reaction, k?, which equals k[Iꢁ]b[Hꢄ]d.
2.2. Instrument and procedure
The measurements of absorbance were carried out
using an RA-401 stopped-flow spectrophotometer (Ot-
suka Electronics Co., Japan). The absorption spectra
could be observed with the minimum time interval of 4
ms after mixing of the reactants. N2 gas used for mixing
is of pressure of 5.0 kg cmꢁ2. The optical cell length is 2
mm and the slit width is 3.5 mm. One of the driving
syringes of the stop-flow unit was filled with KI solution
and the other one was filled with PAA solution. For
each run, equal volumes of both solutions were mixed in
the mixing chamber and the change in the absorbance
due to the generation of I2 with time was monitored at
352 nm [5].
The plot of ln k? versus ln[Iꢁ] should be a straight line
with slope b (which is the order of the reaction with
respect to Iꢁ). While the rate constant of the reaction,
k, can be determined from the intercept at a certain pH.
Similarly the effect of Mo(VI) and pH on the rate of the
reaction can be studied by changing Mo(VI) concentra-
tion or pH and using all the other species in excess.
3.2. Experimental results
3.2.1. Order in PAA
The isolation method was used for the determination
of the order of the reaction with respect to PAA. That is,
Iꢁ was used in a large excess with respect to PAA.
Under these conditions the reaction was expected to be
pseudo-first-order in PAA. Fig. 1 shows the typical
3. Results and discussion
3.1. Theoretical background
absorbanceꢃtime curves at 352 nm for the reaction
/
between 0.22 mM PAA and different concentrations of
KI (the lowest ratio of Iꢁ concentration to PAA
concentration is 25) in 0.05 M acetate buffer solution
(pH 5.4). In each case, the increase in the absorbance is
attributed to the increase in the concentration of the
liberated I2. A leveling of the absorbance occurred after
The overall oxidation of Iꢁ by PAA is expressed as
follows:
k
CH3COOOHꢄ2Iꢁ ꢄ2Hꢄ 0 CH3COOHꢄH2O
Mo(VI)
ꢄI2
(1)
Consequently, the rate of this reaction can be expressed
generally as
rateꢀd[I2]=dtꢀꢁd[PAA]=dt
ꢀk[PAA]a[Iꢁ]b[Mo(VI)]c[Hꢄ]d
(2)
in which Mo(VI) is the possible catalyst of the reaction,
[PAA] is the concentration of PAA, a, b, c and d are the
reaction orders with respect to PAA, Iꢁ, Mo(VI) and
Hꢄ, respectively. aꢄ
/
bꢄ
/
cꢄd then refers to the total
/
order of the reaction. The rate constant for the reaction
can be determined using the isolation method, that is, by
isolating one of the reactants by using the other
reactants in excess. For example, if the initial concen-
trations of the reactants are such that, [Iꢁ]oꢀ
[PAA]o
/
and the experiment is conducted at constant pH and in
the absence of molybdate, then the concentration of Iꢁ
is supposed to be constant during the experiment.
Accordingly, Eq. (2) can be reduced to:
Fig. 1. Typical absorbanceꢃ
/
time curves at 352 nm for the reaction of
acetate buffer solution (pH 5.4). The
ꢁd[PAA]=dtꢀk?[PAA]a; k?ꢀk[Iꢁ]b[Hꢄ]d
(3)
PAA and Iꢁ in 0.5
M
concentration of PAA was kept constant (0.22 mM), while the
concentration of Iꢁ was changed: (1) 10, (2) 12.5, (3) 15.0, (4) 17.5,
(5) 25.0 and (6) 35.0 mM at pH 5.4.
The order of the reaction with respect to PAA can be
then determined using Eq. (3). If the reaction is assumed