the presence of metal ions, arising from the buffer (as traces) or
added in known amounts (Cu2+), was assessed, and the influence
of DAA reactivity on the kinetics was examined.
These findings, besides permitting the rationalization of the
inadequacy of relatively simple kinetic models, can be very helpful
in drawing a reliable picture for the first steps of the quite
complicated reacting system AA-O2.
Modified electrodes showing relatively low ratios (<400)
between the current responses obtained for H2O2 and AA
respectively at the same concentration (1 mM) were not used for
kinetic experiments. This choice was made to minimize the effect
due to the AA electrooxidation products, which could alter the
electrode surface,3,5 thus influencing the sensitivity to H2O2 during
a kinetic run (see also the Results and Discussion session).
Kinetic Measurements. A thermostated electrochemical cell
was used as reaction vessel for all the kinetic experiments in this
work. Particular care was taken to prevent any further introduc-
tion of oxygen (from air) in the reacting system after a run started.
This was mandatory for the experiments involving oxygen, in
which the concentration of dissolved O2 was continuously reduced
during the kinetic run.
Some of the experiments were performed by using, as oxygen
initial concentration, the value corresponding to its partial pressure
in the atmosphere (∼0.19 atm). The concentration was evaluated
to be 0.23 mM, in good agreement with the data reported by Taqui
Khan and Martell4 for an aqueous solution with the same ionic
strength as the buffer used in this work.
EXPERIMENTAL SECTION
Materials. GOx from Aspergillus niger (EC 1.1.3.4, 168 200
units/ g) and ascorbic acid were obtained from Sigma Chemical
Co. (St. Louis, MO) and used as received. Hydrogen peroxide
was obtained as a 36% (w/ v) solution from Carlo Erba (Milano,
Italy). o-Phenylenediamine (o-PD) was purchased from Aldrich
(Steinheim, Germany) and purified just before use by vacuum
sublimation at 90 °C. Pyrrole (Aldrich) was purified by vacuum
distillation at 60 °C and stored under nitrogen at 0 °C.
The buffer solutions (pH ) 7; I ) 0.1) for the kinetic
experiments were always prepared by using monobasic and
dibasic sodium phosphates (ACS reagents) purchased from
Aldrich.
The cell was partially filled with phosphate buffer solution (I
) 0.1, pH ) 7), kept in a thermostatic bath at 27 °C, allowing O2
to reach, under stirring, its equilibrium concentration. The three
electrodes (working, counter, and reference) were then inserted,
and O2 saturated buffer was added to fill the reaction vessel. After
the operating potential (0.7 V vs Ag/ AgCl) was applied and the
system allowed to achieve a steady value for the background
current, the cell was protected from light and the kinetic
experiment started by adding a known amount of AA to the
solution (final concentration ranging from 0.1 to 1 mM). The AA
stock solutions (50 mM) used for the injection were prepared just
before each kinetic run and deaerated by flowing a UHP inert
gas, in order to avoid any preliminary reaction with oxygen.
Other experiments were performed adopting lower oxygen
concentrations. In these cases, a different preparation stage was
necessary before starting the kinetic run. After the cell was filled,
an inert gas was bubbled in the solution through the overflow
pipe until the desired O2 concentration was reached. During this
stage, the O2 concentration was followed (and finally calculated)
by amperometric detection at an additional Pt electrode (operating
potential, -0.4 V vs Ag/ AgCl). The chosen AA aliquot was then
injected and the kinetic study started.
In any case, particular care was used to eliminate small air
bubbles inside the cell before each run.
Kinetic Models. Kinetic models based on two pseudo-first-
order (1/ 1) or second-order (2/ 2) consecutive reactions were
adopted, as a first approach, to study the oxidation of AA by
oxygen and by H2O2 in the same system.
In particular, the 2/ 2 model was chosen on the basis of
previous kinetic investigations1,3,4,6 on processes 1 and 2, indicating
a second-order dependence for their rate.
The mathematical treatment already available7 for this model
(with a ratio of 2 between the initial concentrations of the
reactants) was extended to any ratio between the initial concentra-
tions of the reactants. Briefly, as a final result, the following
equation was obtained:
Apparatus. Modified electrode preparation was carried out
by a PAR 273 potentiostat-galvanostat (EG&G, Princeton Applied
Research, Princeton, NJ) coupled to a conventional three-electrode
system with a Pt wire as counter electrode and a Ag/ AgCl/ KCl
(saturated) electrode as reference. The amperometric response
during kinetic experiments was measured by a Model 400 EC
Detector (EG&G) connected to a Y-t strip chart recorder (LCI
100, Perkin-Elmer, Norwalk, CT).
The UV spectra were recorded in the range 210-400 nm using
a Perkin-Elmer Lambda 2 UV/ visible spectrometer.
Modified Electrode P reparation. The preparation of the
modified electrode has been described elsewhere3. Briefly, a
platinum disk (diameter, 3 mm), embedded in a Teflon cylinder,
was used as the working electrode: its surface was polished with
0.3 µm alumina, washed, and pretreated by potential cycling
between -0.21 and +1.19 V vs Ag/ AgCl in 0.5 M H2SO4 until a
steady state voltammogram was obtained. A PPy film was
potentiostatically grown (at +0.7 V vs Ag/ AgCl) from a 10 mM
KCl solution containing pyrrole (0.4 M). The deposition charge
employed was typically 300 mC/ cm2. The Pt/ PPy-modified
electrode was washed and transferred to another cell containing
5 mM o-PD (and 500 units/ mL of GOx, when indicated) in a 0.1
M phosphate buffer (pH ) 7.0) solution. A potential of +0.7 V
vs Ag/ AgCl was applied in order to potentiostatically deposit a
PPD film; the process was stopped when no appreciable current
flowed in the circuit. After preparation and thorough washing,
the modified electrode was potentiostated at +0.7 V overnight in
a 0.1 M phosphate buffer (pH ) 7.0) in order to complete the
PPy overoxidation process.
A calibration test was performed before each kinetic experi-
ment in order to assess the sensitivity of the Pt/ PPyox/ PPD(GOx)
electrodes to H2O2 in the range 2-100 µM, including the
maximum H2O2 concentrations reached during the reactions. A
response time (t0.9) of about 5 s was estimated. The current values
were controlled to be constant with time, which indicated that no
decomposition of H2O2 was occurring under the present experi-
mental conditions. The rejection of ascorbate from the electrode
surface was also checked by measuring the amperometric
response after addition of AA (final concentration, 1 mM) to
phosphate buffer.
(5) Palmisano, F.; Zambonin, P. G. Anal. Chem. 1 9 9 3 , 65, 2690-2692.
(6) Taqui Khan, M. M.; Shukla, R. S. J. Mol. Catal. 1 9 8 7 , 39, 139-146.
(7) Pannetier, G.; Souchay, P. Chemical Kinetics; Elsevier: Amsterdam, 1967;
pp 196-199.
4114 Analytical Chemistry, Vol. 69, No. 20, October 15, 1997