1818
SARBAEVA et al.
cathodic current maximum corresponding to the
ꢀ0.008
ꢀ0.006
ꢀ0.004
ꢀ0.002
0
reduction of the thallium(I) chloride film formed on
the electrode surface was recorded when the potential
of thallium electrode shifted to negative values, and
the hydrogen ions were reduced at a potential of
−1.4 V. When the electrode potential was shifted in the
positive direction, the anodic current maximum cor-
responding to thallium anodic oxidation was recorded
at potentials of −0.6 to −0.7 V. Up to a potential of
+1.0 V, the voltammetric curve did not show any max-
ima of the subsequent oxidation of thallium ions or the
oxidation of chloride ions.
0.002
0.004
0.4 0.2
0
ꢀ0.2 ꢀ0.4 ꢀ0.6 ꢀ0.8 ꢀ1.0 ꢀ1.2
The concentration of the solution affected the
reaction of thallium electrodissolution. We found that
when the concentration of hydrochloric acid was var-
ied within 0.5–4.0 M, the potential of the thallium
electrode was −0.6 to −0.7 V. When the thallium elec-
trode potential was shifted toward the positive poten-
tial values, the voltammetric curves show that anodic
current values grew with an increase in the concentra-
tion of hydrochloric acid. It was established that at
potentials higher than −0.2 V, the rate of thallium dis-
solution did not grow; from that moment on, a film of
thallium chloride formed on the surface of the metal
dissolving in the transpassive mode. The anodic
curves of thallium oxidation in an aqueous solution of
hydrochloric acid were measured at the potential
sweep rate in the range of 25–250 mV/s (Fig. 2). The
observed oxidation current grew along with the poten-
tial sweep rate.
We calculated two kinetic parameters to character-
ize the electrooxidation of thallium according to Galus
[12]: the diffusion coefficient (D = 8.4 × 10−5 cm2/s)
and the heterogeneous rate constant of the electrode
process (ks = 2.6 × 10−1 s−1). It was established that
thallium does not dissolve anodically in a solution of
hydrochloric acid. When polarized by an industrial
alternating current with a frequency of 50 Hz, it dis-
solves with a high current efficiency with formation of
thallium chloride. We established that under optimum
conditions, monovalent ions form on the surface of a
thallium electrode in the anodic half-period, and
hydrogen is released in the cathodic half-period.
Fig. 1. (Color online) Cathodic/anodic potentiodynamic
cyclic polarization curve in a hydrochloric acid solution;
C = 2.5 M; sweep rate, 250 mV/s; t = 25°С.
distilled water. Hydrochloric acid of analytical grade
and bidistilled water were used to prepare solutions.
Sinusoidal alternating current was supplied from
V-24 power block (basically a step-down transformer
that allowed smooth regulation of the current) with
AC terminals. The current in the circuit was measured
with an ABO-5MI multimeter. Changes in the shape
of the sinusoidal alternating current during electrolysis
were observed using an S1-77 oscilloscope. The oscil-
loscope also was used to observe the ratio of the ampli-
tudes of the anodic and cathodic half-cycles of the
alternating current. A GZM sound-frequency genera-
tor was connected to the setup to study the effect the
frequency of the alternating current had on the rate of
thallium dissolution in an electrochemical circuit.
This allowed electrolysis to be conducted at frequen-
cies from 20 to 20000 Hz. A special YaSE-2 electro-
lytic cell, mounted in an ITZh-0-03 thermostat, was
used for studies at a constant temperature.
The sizes and shapes of the particles of the resulting
thallium(I) chloride were determined on a JSM 6490
LA scanning electron microscope with a magnifica-
tion of ×10000. An LS 13320 laser analyzer with a liq-
uid water module was used to study the size distribu-
tion of thallium(I) chloride particles. The range of
particle size measurement was 0.020 to 200 μm. Laser
light with a wavelength of 750 nm, formed in an ultra-
sonic emitter combined with an LS 13320 unit, was
used to measure the particles via diffraction. X-ray dif-
fraction analysis was performed on a DRON-3.0 dif-
fractometer. The counter rotated at a rate of
2 deg/min.
We studied the effect the density current on a thal-
lium electrode in the formation of thallium(I) ions in
the range of 6000–16000 A/m2 (Table 1). It was found
that thallium does not dissolve at low current densi-
ties. When polarized with an alternating current in a
solution of hydrochloric acid, the rate of thallium dis-
solution with the formation of TlCl increases. For
example, the rate of thallium dissolution at 6000 A/m2
is 83.11 g/(cm2 h). With a current density of
16000 A/m2, it is 198.2 g/(cm2 h). Upon an increase in
the density of alternating current in its anodic half-
period, the rate of oxide film formation slows, and
thallium(I) chloride forms as a result. At high densities
The laws of the dissolution of a thallium electrode
in a solution of hydrochloric acid were preliminarily
established by recording the cathodic, anodic, and
cyclic potentiodynamic polarization curves. The effect
the concentration of hydrochloric acid and the poten-
tial sweep rate had on the reduction of the thallium
electrode was studied. Figure 1 shows the cyclic
cathodic–anodic polarization curve measured on the (above 16000 A/m2), the electrode overheats, and
thallium electrode in hydrochloric acid solution. The electrolysis becomes difficult. Current densities of
RUSSIAN JOURNAL OF PHYSICAL CHEMISTRY A
Vol. 93
No. 9
2019