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of various structural and chemical factors that are important
for their final catalytic properties [8]. The electrodeposition
approach to the production of the Ni–W alloys has also
some apparent advantages, i.e. nanocrystalline/amorphous
materials can be obtained and there is a possibility to control
the grain size of the alloys from several to hundreds of
nanometers. In addition, thin layers of the alloys can be plated
requirement.
2. Experimental procedure
All of the alloys where deposited using an EG&G PARC
galvanostat/potentiostat model 173A. The electrodepositions
were done in a special plating cell, with two symmetrically
placed anodic compartments, separated from the cathodic
chamber with glass frits. Two inert, passivated titanium elec-
trodes (TiO2/RuO2) were used as the anodes. The area of
each anode was circa 10 cm2. Polished Cu–Zn brass and steel
plates and silicon wafers with vapour deposited Cu (Kocour,
Chicago, and Plating Test Cell Supply Company, Cleveland,
OH) had the working area of 2 cm2 and were used as the sub-
strates for the deposits. However, all the results shown in the
figures, except for Fig. 5, were obtained with brass substrates.
Just before plating the substrate was degreased and slightly
etched and activated with dilute sulfuric acid.
For the electrodeposition of the amorphous molybdenum
alloys with the iron-group metals the citrate–ammonia baths
are used in most of the cases [12–16]. However, if the content
of Mo does not exceed 12–13 at.%, the deposits obtained in
the citrate ammonia bath consist of just one crystallographic
phase, i.e. the solid solution of Mo in nickel [13,14]. Then
the structure of the alloy is polycrystalline. When the con-
tent of Mo increases up to 18 at.%, the initial indications of
the formation of the amorphous/nanostructured phase arise.
The alloys become really amorphous/nanostructured when
the content of Mo exceeds 22–25 at.%. The electrodeposi-
tion of such a high-molybdenum-content alloys from the
citrate–ammoniasolutionispossible, however, thevery-high-
molybdenum-content alloys (63 or 38 at.% of Mo), indepen-
The nickel alloys can be also deposited from other baths.
The pyrophosphate bath has been employed for the electrode-
and Sn [20]. A possibility of electrodeposition of the Ni–Mo
alloys from pyrophosphate bath was mentioned some time
ago by Stasov and Pasechnik [21] and recently by Jovic et
al. [22]. The composition proposed in Ref. [21] enables the
deposition of the alloys under reasonable current efficiency
at room temperature with Mo content up to 40 wt.%. The
deposits are well adhered to the copper and steel substrates.
Also, the content of Mo in the alloys does not depend sub-
stantially on temperature in the range 20–40 ◦C. The Ni–Mo
alloys electrodeposited by pulse current [22] might contain
up to 41 at.% of Mo. A current-efficiency drop below 10%
accompanied that high content. Moreover, the morphology
of the deposits was particularly sensitive to the co-evolution
of hydrogen, and most of the deposits exhibited a dense net
of bumps and cracks.
Polarization experiments were done with the three-
electrode system using
a type PI-50-1.1 potentio-
stat/galvanostat, Russia, connected with a PR-8 function
generator. A platinum sheet served as the counter electrode
and a SCE was the reference electrode. The top of a copper
rod of the working area equal to 0.125 cm2 was used as the
working electrode. Before each experiment the surface of
examined solution for 30 min. The ohmic drop was evaluated
in separate experiments by switching the galvanostatic pulse
off after 30 s of electrolysis and measuring the resulting
potential drop with the use of an oscilloscope.
The solution with the main components at the
concentrations such as those reported for the elec-
trodeposition of molybdenum alloys by Stasov and
Pasechnik [21] was the starting point in this work.
Stasov’s solution is called the initial solution through-
out this paper and its composition can be writ-
ten as: Na4P2O7·10H2O—160 g dm−3, NH4Cl—20 g dm−3
,
NiSO4·7H2O—40g dm−3 and Na2MoO4·2H2O. The sug-
gested pH value for the initial solution is 8.5. pH of the final
solutionswasadjustedbyaddingappropriateamountsof30%
ammonium solution. In the course of the work the initial solu-
tion was changed by adding 2-butyne-1,4-diol—50 mg dm−3
and rokafenol N-10 (nonionic detergent)—100 l dm−3, and
by varying the concentration of Na2MoO4 in the bath. All so-
lutions were prepared using deionized water produced by a
NanoPure Milli-Q purification system, Millipore. The alloys
were deposited at 20 ◦C.
The aim of this work was to modify the pyrophosphate
bath so that thin layers of Ni–Mo alloys of good appearance,
integrity and smoothness could be obtained. Such smooth
layers are advantageous from e.g. trybological point of view.
Theaboveaimhasbeenachievedbyadding2-butyne-1,4-diol
and rokafenol N-10 (polyoxyethylene–phenol class nonionic
detergent) to the bath, which compounds were used success-
fully in the electrodeposition of tungsten alloys [23–25]. The
pyrophosphate bath should be more resistive to degradation
(oxidation)comparedtocitrates. Theinfluenceofvariousfac-
tors on the current efficiency, the deposition rate, the molyb-
denum content and the structure of the alloys have been ex-
amined.
Compositions of the deposits were examined using a
Roentec, model M1, EDX analyzer (Germany) integrated
with a LEO, model 435 VP, scanning electron microscope
(SEM). The mean from the multiple EDX composition data,
the weight of the alloy layer and the assumption that six and
two electrons are used in the reduction of the Mo and Ni ions,
respectively, allowed the calculation of the current efficiency.
The deposition rates have been calculated from the difference
in the weight of the substrates after and before deposition.
A NanoScope scanning tunneling microscope (STM) was
used to observe the alloy surfaces and to estimate their