Mohammad N Majeed1, Qahtan A Yousif2, Mahmoud A Bedair3,4. 1. College of Education, Department of Chemistry, University of Al-Qadisiyah, Al Diwaniyah 58001, Iraq. 2. College of Engineering, Department of Materials Engineering, University of Al-Qadisiyah, Al Diwaniyah 58001, Iraq. 3. College of Science and arts, University of Bisha, P.O. Box 101, Al-Namas 61977, Saudi Arabia. 4. Department of Chemistry, Faculty of Science (Men's Campus), Al-Azhar University, Nasr City, 11884 Cairo, Egypt.
Abstract
This study uses nickel nanoparticles coated on the nickel-chromium (Ni-Cr) alloy by the electrodeposition technique to protect the alloy against corrosion. An open-circuit potential and potentiodynamic and linear polarization resistance in a 1 M H2SO4 solution saturated with carbon dioxide were used to study the anticorrosion performance of nanoparticle coatings. When coated with nanomaterials, the corrosion rate of Ni-Cr alloy was lower than when it was bare, and the potential for corrosion increased from -0.433 V for uncoated Ni-Cr alloy to -0.103 V when the electrodes were exposed to saturated calomel. Electrochemical experiments show that nickel-coated Ni-Cr alloy corrosion in sulfuric acid media has high protective characteristics, with an efficiency of 83.69% at 0.165 mA/cm2 current density when pH = 1 is used. As demonstrated by the results of this research, the nickel-chromium alloy can be protected from corrosion in acidic media by a low-acidity bath coating layer. Surface morphologies have shown that coatings at different acidic scales may be able to resist an acid attack because of their excellent adherence to the nickel-chromium alloy surface. Measures for determining and studying the composition of the alloy surface's protective covering were improved using X-ray diffraction (XRD).
This study uses nickel nanoparticles coated on the nickel-chromium (Ni-Cr) alloy by the electrodeposition technique to protect the alloy against corrosion. An open-circuit potential and potentiodynamic and linear polarization resistance in a 1 M H2SO4 solution saturated with carbon dioxide were used to study the anticorrosion performance of nanoparticle coatings. When coated with nanomaterials, the corrosion rate of Ni-Cr alloy was lower than when it was bare, and the potential for corrosion increased from -0.433 V for uncoated Ni-Cr alloy to -0.103 V when the electrodes were exposed to saturated calomel. Electrochemical experiments show that nickel-coated Ni-Cr alloy corrosion in sulfuric acid media has high protective characteristics, with an efficiency of 83.69% at 0.165 mA/cm2 current density when pH = 1 is used. As demonstrated by the results of this research, the nickel-chromium alloy can be protected from corrosion in acidic media by a low-acidity bath coating layer. Surface morphologies have shown that coatings at different acidic scales may be able to resist an acid attack because of their excellent adherence to the nickel-chromium alloy surface. Measures for determining and studying the composition of the alloy surface's protective covering were improved using X-ray diffraction (XRD).
Corrosion is a crucial process that affects
every country’s
economic structure.[1,2] As a result, treating various
alloys separately becomes crucial.[3] Additionally,
corrosion of steel and nickel alloys is a significant industrial hazard
that has garnered considerable attention.[4,5] Due
to their high permeability and low coercivity, nickel alloys are well
suited for soft magnetic applications.[6−8] While nickel–iron
alloys corrode easily when exposed to certain acidic media, these
acidic media are consumed during various manufacturing processes.[9] As a result, maintaining the corrosion resistance
of nickel alloys is a critical and time-consuming work duty.[10] Numerous strategies are used to protect the
metal surface against destructive attacks (anticorrosive approach);
nevertheless, corrosion inhibitors are considered viable to protect
the metal surface, especially in an acidic medium.[11−13] Anions such
as sulfates, nitrates, chlorides, and thiosulfates cause corrosion
damage to iron alloys in the industrial environment, significantly
lowering their operational life.[14−16] Among the several corrosion
protection techniques available, the most successful is the application
of inhibitors and coatings[17−19] Organic corrosion inhibitors,
on the other hand, might be harmful to the environment, producing
cytotoxic and mutagenic damage to biological systems.[20] Surface coating with micro-nano structures can provide
good corrosion protection for metallic matrices.[21] The weak link between the brittle oxide layer and the natural
covering on the metal surface provides insufficient protection against
long-haul consumption.[22,23] Coatings composed of oxide nanoparticles
are frequently used to protect metal substrates against corrosion
in harsh environments.[24,25] The electrodeposition approach
has the following competitive advantages: (a) low energy consumption
for environmental sustainability, (b) rapid industrial scale-up, (c)
simple, cost-effective fabrication, and (d) improved performance and
adaptability due to controllable process parameters such as voltage,
deposition time, current density, bath composition, pH, and temperature.[26−28] Because of their tribological and corrosion-resistant capabilities,
Ni coatings have attracted a lot of interest in the industry.[29] Electrodeposition of nickel (Ni) and reinforcing
nanoparticles was a promising technique for fabricating Ni-based coatings,
with significant advantages such as simple, low-temperature processing,
no need for templates, versatility, cost-effective, rapid process,
mass production, and no need for final product machining.[30] In this study, the nickel alloy turbine blade
specimens were coated with nickel nanoparticles using an electrodeposition
technique at pH scales of 1 and 6. Regrettably, the turbine blades
rusted when cleaned with water in the presence of gaseous byproducts
of heavy fuel burning. It is both economically and environmentally
beneficial. The protection of a nickel alloy was investigated using
electrochemical methods such as open-circuit potential (OCP), potentiodynamic
(PD), electrochemical impedance (EIS), and linear polarization resistance
at a constant temperature (298.15 K) (LPR). To determine the nature
of the coated surface, two surface morphology techniques, field emission
scanning electron microscopy (FESEM) and energy-dispersive X-ray spectroscopy
(EDS), were applied. For this reason, X-ray diffraction (XRD) was
used to supplement the other tests because it is a critical nondestructive
technique for evaluating the alloy’s protective film composition.
Experimental Part
The Ni–Cr alloy samples were
composed of the elements mentioned
in Table . A suitable
sample with the dimensions (1 cm × 1 cm) and thickness specified
below was constructed (0.5 cm). All specimens were polished to a mirror-like
finish using emery sheets of various sizes and then lubricated with
a soft cloth saturated in the diamond paste. The working electrode
of the Ni–Cr alloy was coated with epoxy resin to keep the
exposed area of 1 cm2 away from electrolyte solutions.
An electrolyte solution of 1 molar sulfuric acid in deionized water
saturated with carbon dioxide was used to study the protective effects
of nickel nanoparticles (pH = 1 and 6) on the working electrode surface.
The experiments were conducted at a temperature of 298.15 K.
Table 1
Composition of Ni–Cr Alloy
Specimen
elements
C
Mn
Al
Si
Mo
Fe
Cr
Ni
wt %
0.05
0.12
0.18
2.26
0.03
3.21
15.30
balance
A nickel layer was electrodeposited on Ni–Cr
alloy using
a glass cell with a volume of 250 cm3 and a working electrode
sandwiched between two parallel platinum metal electrodes. The electrodes
were spaced 0.5 cm apart. A magnetic stirrer was used to agitate the
electrolyte, which comprised 40 g/L of nickel chloride hexahydrate,
210 g/L nickel sulfate, and 25 g/L boric acid.[31] Sodium hydroxide was used to adjust the electrolyte’s
pH to 6. The electrodeposition was carried out for 5 min at a steady
DC voltage of 40 V. The electrolyte was kept at a temperature of 308.15
K. The samples were dried in the air for 24 h at ambient temperature
before being stored in a desiccator until further testing. The Ni
layer was deposited onto the Ni–Cr alloy using the identical
technique, except that the electrolyte pH was changed to 1 using nitric
acid. The applied voltage was increased to 60 V for 1.5 min to create
a black nickel layer. The corrosion electrochemical cell was connected
to a potentiostat device to determine full electrochemical parameters.
FESEM (ZEISS Gemini, Germany, Ltd. Company) was employed to characterize
specimens. The chemical components’ compositions were determined
using EDS spectra. The XRD patterns were recorded by the Bruker D6
Advanced diffraction equipment with a Cu radiation source.
Results and Discussion
Open-Circuit Potential (OCP)
The fluctuation can identify
the Ni–Cr alloy coating in OCP as a function of immersion time.
The evolution of the open-circuit potential with time for Ni–Cr
alloy in 1 M H2SO4 solution without and with
coated protection is depicted in Figure . The curves show that the nanomaterial protective
layer causes considerable changes in the OCP’s temporal behavior.
A cathodic displacement of Ni alloy is found in the absence of protection.
However, with nickel layer protection at pH = 6, the potential change
in the cathodic (active) direction is more significant until the 200s.
The decline in OCP is greater at pH = 6 than unprotected, most likely
because the protective layer adequately isolates the Ni–Cr
alloy surface from the corrosive environment. At pH = 1, the profiles
of the OCP curves with nickel coating show typical anodic tendencies.
However, in the latter situation (pH = 1), the OCP values remained
constant, drifting slightly into the 1000s. This could indicate that
an effective protective coating adheres to the alloy’s surface.
Figure 1
OCP curves
without and with coating layers of nickel at pH = 1
and 6 on the Ni–Cr alloy surface.
OCP curves
without and with coating layers of nickel at pH = 1
and 6 on the Ni–Cr alloy surface.
Potentiodynamic Polarization (PDP)
Figure depicts the potentiodynamic
polarization curves of an uncoated Ni–Cr alloy and a nickel-coated
at different pH scales. From these curves, the corrosion potential
(Ecorr), current density value (Icorr), anodic Tafel constant (βa), cathodic
Tafel constant (βc), and corrosion rate (CR) are calculated. Table shows the results
of this calculation. It is common knowledge that samples having a
higher positive corrosion potential are more inert.[17,32] It is clear from Table that the blank shows an Ecorr value of −486.0 mV (vs saturated calomel electrode (SCE)),
while the Ni coatings shift to a more positive Ecorr. The high Ecorr values of
−135.0 mV (vs SCE) and −262.0 mV (vs SCE) are obtained
for the Ni coatings prepared at pH = 1 and 6, respectively, indicating
their resistance to corrosion. It was revealed that the current density
values of the coated sample were lower than those of the uncoated
Ni–Cr alloy, indicating their high corrosion resistance.[33] The corrosion potential of the coated sample
is shifted from the cathodic to the anodic direction. This result
demonstrates the resistance of the coating to corrosive media. Based
on observations of corrosion current density, the following equation
can be used to calculate the percentage of protection efficiency[34] (%PE).where Icorr and I(coating)corr are the corrosion current densities
values in uncoated and coated states, respectively.
Figure 2
Potentiodynamic curves
without and with coating layers of nickel
at pH = 1 and 6 on the Ni–Cr alloy surface.
Table 2
Parameters of Potentiodynamic Curves
without and with Coating Layers of Nickel at pH = 1 and 6 on the Ni–Cr
Alloy Surface
coating types
βa × 10–3 (V/decade)
βc × 10–3 (V/decade)
Icorr (mA/cm2)
Ecorr (mV vs SCE)
corrosion
rate (mpy)
%PE
blank
682.8
295.5
1.65
–486.0
753.7
pH = 1
234.6
115.6
0.19
–135.0
114.30
88.48
pH = 6
111.9
222.0
0.29
–262.0
132.78
82.42
Potentiodynamic curves
without and with coating layers of nickel
at pH = 1 and 6 on the Ni–Cr alloy surface.Corrosion current densities reduced from 1.65 mA/cm2 for the untreated Ni–Cr alloy to 0.12 and 0.29 mA/cm2 for Ni, pH = 1 and Ni, pH = 6, respectively, for the coating
types. The corrosion rate (CR) of nickel coating layers at 132.78
and 114.30 mpy is less than that of the uncoated surface. The Ni coatings
highly reduced the corrosion rate of the Ni–Cr alloy by acting
as a protective layer between the Ni–Cr alloy surface and the
1.0 M of H2SO4 solution.[35] As indicated, the corrosion current density of the nickel-coated
surface at pH = 6 is less than that of the Ni-coated surface at pH
= 1, and the percent PE is more significant. As a result, the enhanced
corrosion protection provided by nickel coatings may be due to the
nickel nanoparticles charged adhering to the electrode surface, shielding
it from corrosive substances such as chloride ions, hydrogen, and
oxygen gas.A thin nickel layer coating applied to the Ni–Cr
alloy surface
in 1 M sulfuric acid solution decreased the cathodic and anodic slopes,
suggesting that the hydrogen production mechanisms were affected by
applying a thin protective film on the alloy surface. Polarization
curves show that both the anode Tafel slopes (βa) and the cathodic
ones (βc) decrease significantly by applying the Ni coating
at different pH values, which suggests that Ni coating mainly inhibits
both the anodic dissolution of the Ni–Cr alloy and the cathodic
hydrogen reduction process to some extent.[36] It is clear that the hydrogen evolution reaction and the metallic
dissolution could be controlled, and the mechanism of the proton discharge
reaction differed depending on the technique of protection utilized.
Linear Polarization Resistance (LPR)
The well-known
linear polarization resistance (LPR) method determines the corrosion
current density. The Stern–Geary equation[37] was utilized to determine the polarization resistance (Rp) of Ni–Cr alloy coatings. From the
(Rp) values obtained from linear polarization
data, the coating protection (LP) was estimated using eq 2,(38) as illustrated in Table ; when a protective
layer is added to the surface, the values of polarization resistance
increase.where Rp0 and Rp are the polarization resistances with and without coating layer,
respectively. The polarization resistance (Rp), the corrosion potential (Ecorr), the corrosion current density (Icorr), and the corrosion rate are determined by doing a linear regression
on a current density versus potential curve near the corrosion potential.
Thus, the corrosion rate of a Ni–Cr alloy with a coating layer
is 75 mpy (at pH = 1), while the corrosion rate of the alloy surface
without a coating is around 462.5 mpy.
Table 3
LRP Method Information without and
with Coating Layers of Nickel at pH = 1 and 6 on the Ni–Cr
Alloy Surface
coating types
Icorr (A/cm2)
–Ecorr (mV)
Rp (Ω cm2)
corrosion
rate (mpy)
%LP
blank
1.012 × 10–3
433.1
25.74
462.5
Ni, pH = 1
165.9 × 10–6
103
157
75.82
83.69
Ni, pH = 6
225.4 × 10–6
247
115
103
77.61
According to Table , the nickel coating is more resistant to corrosion
at a low pH value
than its Ni-alloy counterpart at a high acidic value, owing to the
higher Rp values of 157 and 115 Ω
cm2, respectively. At pH = 1, nickel coatings exhibit the
most remarkable polarization resistance and the slowest corrosion
rate. According to Table , the corrosion potential of coating layers increases as they
become nobler. In comparison, the corrosion potential of the blank
was −433.1 mV, indicating a more potent negative direction
of corrosion.
Electrochemical Impedance Measurements (EIS)
Electrochemical
impedance measurements were made to better understand the Ni–Cr
alloy surface electrode’s behavior. Figures and 4 show the Bode
and Nyquist plots for a Ni–Cr alloy surface immersed in 1 M
H2SO4 and nickel layers plated on the Ni-alloy
surface. The diameter of the semicircle fluctuates, and modifications
are made in response to changes in the coating pH scale. The deviation
from the perfect semicircle is typically caused by frequency dispersion,
surface inhomogeneity, coating grain boundaries, and solution contaminants.[39−41]Figure A illustrates
the equivalent circuit used to fit the electrochemical impedance spectroscopy
of Ni–Cr alloy in 1 M H2SO4 with and
without the coated layer.
Figure 3
Bode curves without and with coating layers
of nickel at pH = 1
and 6 on the Ni–Cr alloy surface.
Figure 4
Nyquist curves without and with coating layers of nickel
at pH
= 1 and 6 on the Ni–Cr alloy surface.
Figure 5
Equivalent circuit model to fit EIS spectra (A) measurement
and
calculation fitting curves of blank (B), and coating layers of nickel
at pH = 1 (C), and pH = 6 (D) on the Ni–Cr alloy surface.
Bode curves without and with coating layers
of nickel at pH = 1
and 6 on the Ni–Cr alloy surface.Nyquist curves without and with coating layers of nickel
at pH
= 1 and 6 on the Ni–Cr alloy surface.Equivalent circuit model to fit EIS spectra (A) measurement
and
calculation fitting curves of blank (B), and coating layers of nickel
at pH = 1 (C), and pH = 6 (D) on the Ni–Cr alloy surface.Table summarizes
the impedance characteristics of the electrolyte “solution”
resistance (Rs), pore resistance (Rpore), and charge transfer resistance (Rct). The constant phase parameters Ycoating, m and Ycorr, n refer to the coating layer and corrosion
reaction “double layer,” respectively. The following
equation was used to determine the percentage protection efficiency[42,43] (%Epr).where Rct,c and Rct are the charge transfer resistance with and
without coating layers, respectively.
Table 4
EIS Data of without and with Coating
Layers of Nickel at pH = 1 and 6 on the Ni–Cr Alloy Surface
coating types
blank
Ni, pH = 1
Ni, pH = 6
Rs (Ω)
4.102
3.094
3.76
Rpore (Ω)
15.62
88.57
3.099
Rct (Ω)
23.07
118.7
78.38
Ycoating (S – sm) ×
10–6
7.874
104.6
18.01
n ×
10–3
704
882.4
987
Ycorr (S – sn)
1.226 × 10–3
2.124 × 10–3
708.2 × 10–6
m ×
10–3
492
556
678
Cd1 (μF/cm2)
3.259 × 10–3
1.80 × 10–5
3.79 × 10–5
%Epr
80.564
70.566
Additionally, Table provides the double-layer capacitance per unit electrode
area (Cdl) and the double-layer capacitance
per unit
electrode area (Cdl,coating) determined
from the curves presented in Figure . The n exponent values in Table range between 0.704 and 0.978, demonstrating
nonideal capacitance behavior induced by the heterogeneity[44,45] of Ni–Cr alloy surfaces generated by the stiffness of the
surface coating layer. The resistances have changed because Rpore replaces the protective layers and Rct is increased and lowers the Rs value.It indicates the protective layer’s
thickness. It reduces Cdl by increasing
the thickness of the electrical
double layer,[46,47] suggesting that the nickel layer
at pH = 1 provides the optimum protection for the alloy under optimal
conditions. As depicted in Figure , the Bode diagram demonstrates that as the protective
coating layer changes, the |Z| and phase angles rise,
implying that it supports a single charge transfer mechanism. At pH
= 1, the capacitance of the double layer decreases, indicating that
the amount of Ni–Cr alloy components dissolving has been reduced.Additionally, the capacitance value of the coating is significantly
lower, demonstrating the coating’s compact nature. As shown
in Table , as the
pH of the coating bath was dropped to prepare the layers on the working
electrode surface, the protective efficiency increased. On the other
hand, these findings show that the nickel alloy surface coating’s
barrier properties are strengthened, consistent with potentiodynamic
and linear polarization data investigations.
Surface Analysis Techniques
Figure shows FESEM images and an EDX spectrum of
the uncoated alloy and nickel coatings at different pH scales for
the Ni–Cr alloy electrode surface. Image A demonstrates uncoated
Ni–Cr alloy. The nickel layer deposited on the surface alloy
at pH = 1 is shown in Figure b. It demonstrates that the coatings created on the nickel
alloy surface are more homogeneous and denser. The coating is of such
high quality that no cracks or separation of the coatings with visible
superficial cracks is due to the density of the deposited layer. Image
C demonstrates that the nickel coating (pH = 6) is brittle and insufficiently
cohesive, revealing a change in the acidity of the electroplating
bath; it is assumed that this resulted in insufficient adherence to
the alloy’s surface.
Figure 6
FESEM images and EDX of blank (A) and coating
layers of nickel
at pH = 1 (B) and pH = 6 (C) on the Ni–Cr alloy surface.
FESEM images and EDX of blank (A) and coating
layers of nickel
at pH = 1 (B) and pH = 6 (C) on the Ni–Cr alloy surface.The EDS elemental analysis shown in Figure B indicates a higher Ni content
related to
the type of coating layer. It is relatively lower in the presence
of a coating layer at pH = 6. Besides, the Ni element was detected
by the EDX analysis in the uncoated alloy related to the composition
of the alloy without any percent for the chromium element.
X-ray Diffraction (XRD)
The X-ray diffraction peaks
were recorded and are presented in Table to identify the protective layer’s
porous alloy surface and crystalline phases. The peaks at 36.47, 44.31,
51.48, 54.94, and 75.73°, respectively, can be indexed to the
diffractions of (202), (111), (200), (242), and (220) Miller planes,
as shown in Figure .
Table 5
XRD Analysis Peaks of Ni–Cr
Alloy Surface and Coating Layers of Nickel at pH = 1 and 6
peak position
(2θ)
FWHM (β)
theta (θ)
intensity
crystallite
size D (nm)
Miller index
36.473
1.180
18.236
0033
07.23
202
44.313
0.344
22.156
1164
25.42
111
51.488
0.393
25.744
0532
22.87
200
54.949
0.590
27.474
0033
15.48
242
75.733
0.246
37.866
0568
41.75
220
Ni, pH = 1
44.2089
0.3444
22.10445
1501
25.41
111
51.4195
0.3936
25.70975
656
22.87
200
75.6341
0.3936
37.81705
568
26.08
220
Ni, pH = 6
44.0136
0.3444
22.0068
3118
25.40
111
51.2041
0.3936
25.60205
1319
22.84
200
75.5337
0.3936
37.76685
568
26.06
220
Figure 7
X-ray diffraction pattern of Ni–Cr alloy surface and coating
layers of nickel at pH = 1 and 6.
X-ray diffraction pattern of Ni–Cr alloy surface and coating
layers of nickel at pH = 1 and 6.The pattern shows that the porous material is made
of nickel at
a high intensity due to the high solubility of chromium atoms in the
nickel matrix. Figure shows the XRD patterns of nickel plating at pH = 1 and 6. The thin
crystallinity and purity of the nickel nanoparticles were further
confirmed by the diffraction peaks’ vulnerability and the absence
of any diffraction peak matching any impurity.As seen in Table , the Ni coating layers
were responsible for the high diffraction
peaks at ≈44, ≈51, and ≈75°. The XRD pattern
(Figure ) of pH =
1 displays the same diffraction peaks as pH = 6 with different intensities,
as shown in Table . At pH = 1 and 6, nickel nanoparticles had particle diameters of
24.78 nm and 24.76 nm, respectively. The findings demonstrated no
further variations in the particle sizes of the protective layer generated
on the Ni–Cr alloy surface using the electrodeposition approach,
even though previous electrochemical methods revealed an obvious shift
in protection.
Conclusions
The investigations described in this work
indicate that nickel
nanoparticles with a pH of 1 are an excellent coating that was successfully
formed on a Ni–Cr alloy specimen using the electrodeposition
method, exhibiting excellent corrosion resistance in sulfuric acid
solution (1 M) saturated with CO2. Electrochemical studies
revealed that nickel coatings on the alloy surface reduce corrosion
current densities and increase polarization resistance in corroded
acidic solutions. Under fixed voltage, it takes less time to achieve
a uniform, compact, and adherent nickel coating. Electrochemical impedance
spectroscopy measurements were used to determine the resistance of
the protective layer coating. The values for the coatings are significantly
higher than those for the bare alloy. The EIS results are consistent
with those obtained from potentiodynamic and linear polarization measurements.
This study demonstrates that nickel coatings with a pH of 1 layer
exhibit excellent corrosion resistance and can be considered a potential
coating material for protecting Ni–Cr alloy from corrosion
in a 1 M H2SO4 solution. These observations
are confirmed by FESEM, EDX, and XRD analyses.