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density at potentials more negative than about −0.840 V.
Analysis of the partial current density curves indicated that,
under the experimental conditions used, the maximum can-
not be attributed to hydrogen reduction only. This inhibition
is probably the cause of the abrupt change in potential, alloy
composition and current efficiency observed during galvano-
static electrodepositions when the current density applied
drives the cathodic potential in this range. At potentials more
negative than about −1.000 V, depending on the experimental
conditions, the equilibrium potential of zinc is reached and
very zinc-rich alloys are obtained, due to the large differences
between the exchange current densities of zinc and nickel or
cobalt [9–11].
Both for Zn–Co and Zn–Ni alloys, the deposition of alloys
of different composition, morphology and structure depend-
ing on the cathodic potential was observed [4,6]. In particular,
the maximum in the polarization curve, obtained by plotting
as a function of the potential the stationary values of j mea-
sured during potentiostatic electrodepositions, coincideswith
a maximum in the internal stress of the deposits [4,6]. Previ-
ous results on Zn–Co alloy [4] showed that X-ray analysis is
not always able to identify the deposited phases because this
alloy is poorly crystallized in a wide range of composition,
with a large amount of crystallites too small for resolution by
this technique.
The aim of this work was to study the Zn–Co alloy
electrodeposition from chloride baths without complexing
agents by cyclic voltammetry (CV) and anodic linear sweep
voltammetry (ALSV), to identify the deposited phases at the
various potentials and to investigate the cause of the inhi-
bition observed at low polarizations. Scanning electronic
microscopy (SEM) and transmission electronic microscopy
(TEM) observations together with energy dispersive X-ray
(EDX) analysis were carried out on some deposits obtained
potentiostatically. The attention was particularly focused on
the range of potential where zinc deposits underpotential.
platinum substrate was used because the corrosion potential
of iron in the deposition bath (−0.600 V versus Ag/AgCl)
is lower than that of cobalt and cobalt-rich alloy dissolu-
tion potential. Stripping analysis was performed immediately
after potentiostatic depositions at different potentials without
removing the electrode from the solution and selecting, in
each case, an initial potential for which deposition did not
occur. The deposition and stripping charges were calculated
by integrating the current/time curves. All the potentiody-
namic polarizations were carried out using a scanning rate
of 5 mV s−1, chosen after preliminary tests. A conventional
three-electrode cell was used. The working electrode was
mounted in a flat specimen holder with an exposed area of
0.71 cm2; the counter-electrode was a platinum spiral and the
reference electrode was a Ag/AgCl electrode, mounted inside
a Luggin capillary, whose tip was placed next to the working
electrode surface. Before each experiment, solutions were
deaerated with N2 inside the cell. Electrochemical measure-
ments were performed using an EG & G Princeton Applied
Research potentiostat/galvanostat Mod. 273 controlled by a
personal computer. In order to determine the percentage com-
position of the electrodeposited alloys, some deposits were
stripped in a minimum volume of 1:3 HCl solution and anal-
ysed for cobalt and zinc by means of an inductively coupled
plasma spectrometer (Perkin-Elmer Optima 3200 XL).
The deposits obtained potentiostatically were character-
ized by means of a Philips XL 20 scanning electron micro-
scope and an energy-dispersive X-ray spectrometer (Edax
PV9800). The phases of the deposit obtained potentiostati-
cally at −0.96 V were identified by means of a Philips CM
200 transmission electron microscope.
3. Results and discussion
Potentiostatic electrodepositions in the potential range
from −0.760 to −1.100 V were performed on iron and plat-
inum cathodes from the bath containing 0.19 M Co2+ and
0.40 M Zn2+ (Co2+ percentage in the bath (Cob): 30 wt.%),
in order to study the effect of the change in substrate. The
results indicated that the change in substrate does not signif-
icantly affect the polarization curves and the composition of
the deposits (Fig. 1). On the contrary, some tests performed
on glassy carbon electrode showed a strong decrease in the
the electrode surface was totally covered by the alloy. These
results agree with those of other authors [8,12] that found a
strong inhibition of the process on glassy carbon cathode.
Fig. 2 shows the cyclic voltammogram obtained from the
same bath used for the potentiostatic tests. The scan was
started from the rest potential of Pt (−0.100 mV) and reversed
at −1.100 V. The curve shows that the alloy deposition starts
at about −0.750 V, according to the potentiostatic tests results
(Fig. 1); the cathodic current peak, observed in the polar-
ization curve obtained by means of the potentiostatic tests
(Fig. 1), is a complex peak with one maximum (C2) and
2. Experimental details
Zn–Co alloy potentiostatic electrodepositions were car-
ried out at 55 ◦C for 200 s, using a bath of the
following composition: 54.57 g dm−3 (0.40 M) ZnCl2;
45.30 g dm−3 (0.19 M) CoCl2·6H2O; 26 g dm−3 (0.42 M)
H3BO3; 220 g dm−3 (2.95 M) KCl (pH 4.2). This bath was
chosen in order to correlate of the present results with those
obtained previously [4]. Cyclic voltammetry was carried out
from similar baths, changing the concentrations of Zn2+ (0,
0.0015, 0.015, 0.1 and 0.4 M) or Co2+ (0, 0.002, 0.02, 0.1 and
0.19 M), while maintaining constant Co2+ (0.19 M) or Zn2+
(0.4 M) concentrations, respectively. All the solutions were
prepared with doubly distilled water and analytical grade
reagents.
Potentiostatic electrodepositions were carried out on mild
steel and platinum disks. Cyclic voltammetry and anodic lin-
ear sweep voltammetry were performed on a platinum disk; a