3.1 The structure, composition, morphology and property of Co-Mo coating
3.1.1 Effect of the concentration of Na2MoO4
The XRD spectra of the Co-Mo coatings at different concentrations of Na2MoO4 are shown in Fig. 1(a). The XRD spectra of the coatings with different concentrations of Na2MoO4 showed a broad diffraction peak around 2θ = 43°, indicating that the Co-Mo coating is an alloy with an amorphous structure. The XRD spectra of the coatings prepared with the concentration of Na2MoO4 at 0.075 mol/L, 0.1 mol/L, 0.125 mol/L and 0.15 mol/L show the diffraction peak of copper at 2θ = 50° and 2θ = 74°, and a less obvious broadened diffraction peak is shown near 2θ = 43°. Combined with electrochemical test of different concentrations of Na2MoO4, it was shown that as the concentration of Na2MoO4 increases, the deposition of alloy becomes more and more difficult, so the coating becomes thin, causing X-rays to hit the copper substrate.
Figure 1(b) shows the influence of the concentration of Na2MoO4 in the plating solution on the composition and current efficiency of the Co-Mo coatings. As the concentration of Na2MoO4 increases, the mass fraction of molybdenum in the coating shows a trend of first decreasing and then increasing. When the concentration of Na2MoO4 in the plating solution is 0.05mol/L, the content of molybdenum reaches the maximum value of 37.25%. It is reported that the greater the concentration of Na2MoO4 in the plating solution in a certain range, the higher the content of molybdenum in the coating. However, the electrochemical test results of different sodium molybdate concentrations shows that as the concentration of Na2MoO4 increases, the exchange current density i0 decreases, the charge transfer resistance Rct increases, which is conducive to the separate deposition of cobalt and hinders the co-deposition of cobalt and molybdenum. At the same time, as the concentration of Na2MoO4 increases, the thickness of the coating becomes thinner, resulting in the determination of the mass fraction of coating components, the copper matrix also occupies a certain mass fraction.
As the concentration of Na2MoO4 in the plating solution increases, the current efficiency decreases. This is because as the concentration of Na2MoO4 increases, the deposition of alloy becomes difficult and the coating quality decreases. According to the Eq. (2 − 1), the current efficiency decreases.
The surface morphology of the Co-Mo coating under different concentrations of Na2MoO4 is shown in Fig. 2. When the concentration of Na2MoO4 is 0.05 mol/L, the Co-Mo coating has the characteristics of the surface morphology of nodular shape, the surface is flat and smooth, and the crystal grains are small and uniform. This is due to the higher content of molybdenum in the coating. When the concentration of Na2MoO4 increases, the surface quality of the coating is reduced, the surface becomes uneven, and the crystal grains become coarse.
Figure 3 shows the comparison of the microhardness of the Co-Mo coating with different concentrations of Na2MoO4. As the concentration of Na2MoO4 in the plating solution increases, the microhardness of the Co-Mo coating is reduced. When the concentration of Na2MoO4 is 0.075 mol/L, 0.1 mol/L, 0.125 mol/L and 0.15 mol/L, The microhardness of Co-Mo coating are 289.486HV、268.462 HV、240.938 HV、207.722 HV. When the concentration of Na2MoO4 is 0.05 mol/L, the microhardness of the Co-Mo coating reaches the maximum value of 331HV.
From the perspective of the structure of coating, the coating is an amorphous alloy, indicating that molybdenum enters the cobalt lattice, causing lattice distortion, which hinders the movement of dislocations and improves the microhardness of the coating. Therefore, the higher the content of molybdenum in the coating, the higher the microhardness. Moreover, as the concentration of Na2MoO4 increases, the thickness of the coating decreases. During the microhardness test, the diamond probe may release the copper matrix. The microhardness of copper is about 200HV, which makes the microhardness of the coating low.
3.1.2 Effect of the concentration of C6H5Na3O7
The XRD spectra of the Co-Mo coatings at different concentrations of C6H5Na3O7 are shown in Fig. 4(a). The XRD spectra of the coatings with different concentrations of C6H5Na3O7 showed a broad diffraction peak around 2θ = 43°. The XRD spectra of the coatings prepared with the concentration of C6H5Na3O7 at 0.2 mol/L, 0.25 mol/L and 0.3 mol/L show the diffraction peak of copper at 2θ = 50° and 2θ = 74°, and a less obvious broadened diffraction peak is shown near 2θ = 43°. Combined with electrochemical test of different s concentrations of C6H5Na3O7, it was shown that when the concentration of C6H5Na3O7 is too high, the deposition of alloy becomes difficult, so the coating becomes thin, causing X-rays to hit the copper substrate.
Figure 4(b) shows the influence of the concentration of C6H5Na3O7 in the plating solution on the composition and current efficiency of the Co-Mo coatings. As the concentration of C6H5Na3O7 increases, the mass fraction of molybdenum in the coating shows a trend of first increasing and then decreasing. When the concentration of C6H5Na3O7 in the plating solution is 0.15mol/L, the content of molybdenum reaches the maximum value of 37.25%. The deposition of molybdenum mainly depends on the formation of cobalt-molybdenum complex ions. Combined with the electrochemical test results, when the concentration of C6H5Na3O7 in the solution is too low, the optimal concentration for forming complex ions cannot be achieved, which is not conducive to the deposition of molybdenum. When the concentration of C6H5Na3O7 increases to 0.15 mol/L, the exchange current density reaches the maximum value and the charge transfer resistance reaches the minimum value. At this time, the deposition of alloy is easier, and the content of molybdenum in the coating reaches the maximum value. With the further increase of the C6H5Na3O7 concentration, excessive ions hinder the movement of complex ions to the cathode, the exchange current density begins to decrease, the charge transfer resistance begins to increase, alloy deposition becomes difficult, and the molybdenum content in the coating decreases.
As the concentration of C6H5Na3O7 in the plating solution increases, the current efficiency increases first and then decreases. This is because as the concentration of C6H5Na3O7 increases, the deposition of alloy becomes easy and the coating quality increases, according to the Eq. (2 − 1), the current efficiency increases. However, as the concentration of C6H5Na3O7 further increases, the deposition of the alloy is hindered, and the quality of the coating decreases. According to the Eq. (2 − 1), the current efficiency decreases.
The surface morphology of the Co-Mo coating under different concentrations of C6H5Na3O7 is shown in Fig. 5. When the concentration of C6H5Na3O7 is 0.1 mol/L, the Co-Mo coating has the characteristics of the surface morphology of irregular polygonal flakes. When the concentration of C6H5Na3O7 is 0.15 mol/L, the surface is flat and smooth, and the crystal grains are small and uniform. This is due to the higher content of molybdenum in the coating. When the concentration of C6H5Na3O7 continue to increase, the surface becomes uneven, and the crystal grains become coarse.
Figure 6 shows the comparison of the microhardness of the Co-Mo coating with different concentrations of C6H5Na3O7. As the concentration of Na2MoO4 in the plating solution increases, the microhardness of the Co-Mo coating increases first and then decreases. When the concentration of C6H5Na3O7 is 0.1mol/L, 0.2 mol/L, 0.25mol/L and 0.3mol/L, the microhardness of Co-Mo coating is 314HV, 284.4HV, 270.2HV and 251.6HV, respectively. When the concentration of C6H5Na3O7 is 0.15 mol/L, the microhardness of the Co-Mo coating reaches the maximum value of 331HV. As the concentration of C6H5Na3O7 increases, the content of molybdenum in the coating first increases and then decreases, and the degree of lattice distortion caused first increases and then decreases. Therefore, the microhardness of the coating first increases and then decreases.
3.1.3 Effect of the pH value
The XRD spectra of the Co-Mo coatings under different pH are shown in Fig. 7(a). The XRD spectra of the coatings under different temperature showed a broad diffraction peak around 2θ = 43°. The XRD spectra of the coatings prepared with the pH at 6 and 9 show the diffraction peak of copper at 2θ = 50° and 2θ = 74°, and a less obvious broadened diffraction peak is shown near 2θ = 43°. Combined with electrochemical test of different temperature, it was shown that as the pH rises, the deposition of alloys becomes more difficult, but when the pH is 6, the alloy deposition rate is too fast, and the hydrogen evolution reaction is violent due to the high concentration of H+ in the electroplating solution, causing the coating surface to fall off causing the coating surface to peel off, which makes the coating thinner causing X-rays to hit the copper substrate.
Figure 7(b) shows the influence of the pH on the composition and current efficiency of the Co-Mo coatings. As the pH increases, the mass fraction of molybdenum in the coating shows a trend of decreasing. When the pH is 6, the content of molybdenum reaches the maximum value of 38.98%. Combined with the electrochemical test results, as the pH increases, the exchange current density decreases, and the charge transfer resistance increases, which makes the deposition of alloy more difficult, so the content of molybdenum in the coating decreases.
As the pH increases, the current efficiency increases first and then decreases. When the pH is 7, the current efficiency reaches the maximum value. The low current efficiency is due to the high content of molybdenum. The deposition of MoO42− is not a one-step reduction to Mo. The first stage is the reduction of MoO42− to low-valent molybdenum oxides, such as MoO2, under the action of CoCit−. At this stage, there is a hydrogen evolution reaction, so this leads to a decrease in current efficiency[22]. Therefore, when the pH is 6, the current efficiency is low. However, when the pH is too high, the deposition quality is reduced, resulting in a decrease in current efficiency.
The surface morphology of the Co-Mo coating under different pH is shown in Fig. 8. As the pH rises, the surface of the coating becomes smoother and the crystal grains are smaller. When the pH is 8 and 9, the Co-Mo coating has the characteristics of the surface morphology of irregular polygonal flakes. This is due to the lower content of molybdenum in the coating.
Figure 9 shows the comparison of the microhardness of the Co-Mo coating under different pH. As the pH increases, the microhardness of the Co-Mo coating increases first and then decreases. When the pH is 6, 8 and 9, the microhardness of Co-Mo coating are 276 HV、269.46 HV、245.93 HV. When the pH is 7, the microhardness of the Co-Mo coating reaches the maximum value of 331HV. The higher the content of molybdenum in the coating, the greater the hardness of the coating. When the pH is 6, although the content of molybdenum in the coating is high, the surface of the coating falls off, causing the diamond probe to contact the copper substrate during the microhardness test, which makes the microhardness of the coating lower.
3.1.4 Effect of the temperature
The XRD spectra of the Co-Mo coatings under different temperature are shown in Fig. 10(a). The XRD spectra of the coatings under different temperature showed a broad diffraction peak around 2θ = 43°. The XRD spectra of the coatings prepared with the temperature at 40℃, 55℃and 60℃ show the diffraction peak of copper at 2θ = 50° and 2θ = 74°, and a less obvious broadened diffraction peak is shown near 2θ = 43°. Combined with electrochemical test of different temperature, it was shown that as the temperature rises, the deposition of the alloy becomes easier, but when the temperature is too high, the deposition rate is too fast, causing the coating surface to peel off, which makes the coating thinner causing X-rays to hit the copper substrate.
Figure 10(b) shows the influence of the temperature on the composition and current efficiency of the Co-Mo coatings. As the temperature increases, the mass fraction of molybdenum in the coating shows a trend of first increasing and then decreasing. When the temperature is 50℃, the content of molybdenum reaches the maximum value of 39.56%. The deposition of molybdenum mainly depends on the formation of cobalt-molybdenum complex ions. Combined with the electrochemical test results, as the temperature increases, the migration rate of complex ions to the cathode increases, the exchange current density increases, and the charge transfer resistance decreases, which makes the deposition of alloy easier, so the content of molybdenum in the coating increases. However, when the temperature is too high, it will affect the stability of the complex ions, which is not conducive to the deposition of molybdenum, resulting in a decrease in the content of molybdenum in the coating.
As the temperature increases, the current efficiency increases first and then decreases. When the temperature is 50℃, the current efficiency reaches the maximum value of 63%. This is because as the temperature increases, the deposition of alloy becomes easy and the coating quality increases, according to the Eq. (1), the current efficiency increases. However, as the temperature further increases, the deposition rate is too fast, causing the coating surface to fall off and reduce the quality, according to the Eq. (2 − 1), the current efficiency decreases.
The surface morphology of the Co-Mo coating under different temperature is shown in Fig. 11. When the temperature is 40℃, the Co-Mo coating has the characteristics of the surface morphology of irregular polygonal flakes. As the temperature rises, the surface of the coating becomes smoother and the crystal grains are smaller. This is due to the higher content of molybdenum in the coating. When the temperature is too high, the surface becomes uneven, and the crystal grains become coarse.
Figure 12 shows the comparison of the microhardness of the Co-Mo coating under different temperature. As the temperature increases, the microhardness of the Co-Mo coating increases first and then decreases. When the temperature is 40℃, 45℃, 55℃ and 60℃, the microhardness of Co-Mo coating are 320HV, 314HV, 397HV and 376HV. When the temperature is 50℃, the microhardness of the Co-Mo coating reaches the maximum value of 503HV. As the temperature increases, the content of molybdenum in the coating first increases and then decreases. The thickness of the coating also increases first and then decreases. Therefore, the microhardness of the coating first increases and then decreases.
3.1.5 Characterization of coating surface elements
XPS was used to test the composition and chemical valence state of the Co-Mo coating. XPS pattern of (a) full spectrum of elements, (b) Co2p, (c) O1s and (d) Mo3d of Co-Mo coating is shown in Fig. 13. As shown in Fig. 13 (a), the peaks of O, Co and Mo appear in the spectrum. As shown in Fig. 13 (b), the Co 2p1/2 XPS has two split peaks, belonging to Co (799.3 eV), Cobalt Oxides (804.1 eV). The Co 2p3/2 XPS has two split peaks, belonging to Co (779.1 eV), Cobalt Oxides (781.7 eV). Coating surface formed an oxide film when exposed to air. As shown in Fig. 8 (c), the O 1s XPS has one split peaks at 532.3 eV, which is related to the Er2O3 and the metal oxide. As shown in Fig. 8 (d), the Mo 3d XPS has three split peaks, belonging to Mo6+ (235.5 eV), Mo3+ (228.9 eV and 232.3 eV). The existence of Mo6+ is due to the oxidation of Mo to MoO3 and the existence of Mo3+ is due to the oxidation of Mo to Mo2O3.As shown in Fig. 14, it can be seen that the distribution of Co and Mo elements is very uniform. Figure 14(b) shows the EDS spectrum and the composition of the Co-Mo coating, the peaks of Co and Mo appear on the EDS pattern.
3.2 The electrochemical behavior of the deposition of Co-Mo alloy
3.2.1 Deposition potential
Figure 15(a) shows the cyclic voltammetry curves of cobalt-molybdenum plating solutions with different concentrations Na2MoO4 on glassy carbon electrodes. When the concentration of Na2MoO4 is 0.05 mol/L, 0.075mol/L, 0.1 mol/L, 0.125mol/L and 0.15 mol/L, the reduction peak appears at -0.85V, -0.9V, -0.95V, -1V and − 1.05V during the negative scan, and the oxidation peak appears at -0.25V, -0.3V,-0.33V and − 0.35V during the positive scan. Figure 15(b) shows the cyclic voltammetry curves of cobalt-molybdenum plating solutions with different concentration of C6H5Na3O7 on glassy carbon electrodes. When the concentration of C6H5Na3O7 is 0.1 mol/L, 0.15 mol/L, 0.2mol/L, 0.25mol/L and 0.3mol/L, the reduction peak appears at -0.85V, -0.75V, -0.9V, -0.95V and − 1V during the negative scan, and the oxidation peak appears at -0.25V, -0.1V, -0.3V, -0.35V and − 0.38V during the positive scan. Figure 15(c) shows the cyclic voltammetry curves of cobalt-molybdenum baths with different pH on glassy carbon electrodes. When the pH is 5, 6, 7 and 8, the reduction peak appears at -0.75V, -0.8V, -0.9V and − 1V when scanning in the negative direction, and the oxidation peak appears at -0.15V, -0.25V, -0.3V and − 0.35V when scanning in the forward direction. When the pH is 9, there is almost no redox peak. Figure 15(d) shows the cyclic voltammetry curves of cobalt-molybdenum baths with different temperature on glassy carbon electrodes. When the temperature is 40℃, 45℃, 50℃, 55℃ and 60℃, the reduction peak appears at -0.89V, -0.87V, -0.85V, -0.84V and − 0.82V when scanning in the negative direction, and the oxidation peak appears at -0.25V, -0.26V, -0.27V, -0.29V and − 0.32V when scanning in the forward direction.
It can be seen from the CV graph that as the concentration of Na2MoO4 increases, the deposition potential of the cobalt-molybdenum alloy moves in a negative direction. The reason for this trend is that when the concentration of Na2MoO4 increases, too much molybdate ions make the migration rate of complex ions slow, and the precipitation potential shifts in the negative direction; as the concentration of C6H5Na3O7 increases, the deposition potential of the cobalt-molybdenum alloy first shifts to a positive direction and then to a negative direction. The reason for this trend is that when the concentration of C6H5Na3O7 increases, the number of cobalt-molybdenum complex ions formed increases, which facilitates the deposition of cobalt-molybdenum complex ions, thereby shifting the precipitation potential to the positive direction. When the concentration of C6H5Na3O7 is high, the ionization equilibrium is destroyed, resulting in the pH of the plating solution; as the pH increases, the deposition potential of the cobalt-molybdenum alloy shifts in the negative direction. The reason for this trend is that when the pH value is high, Co(Ⅱ) exists in the form of CoCit−, and molybdenum exists in the form of MoO42−; when the pH value is low, Co(Ⅱ) exists in the form of HCoCit, molybdenum exists in the form of HrMoO4Cit[5−r] [11]; as the temperature rises, the deposition potential of the cobalt-molybdenum alloy shifts in the positive direction. This is because as the temperature rises, the migration rate of ions increases, and the stability of complex ions is destroyed, so it is more conducive to the deposition of cobalt, and the deposition potential moves forward.
3.2.2 Exchange current density
The exchange current density is an important kinetic parameter to evaluate the electrode reaction: The higher the exchange current density, the easier the electrode reaction. Therefore, the exchange current density i0 on the glassy carbon electrode in the bath was studied by LSV. The Butler-Volmer[23, 24] equation was applied at very low cathode overpotential, which can be simplified to Eq. (2), Take the logarithm of both sides of Eq. (2) to obtain Eq. (3).
$$i={i}_{0}\left\{-exp\left[\frac{-\alpha nF}{RT}\eta \right]\right\}$$
2
$$\text{l}\text{o}\text{g}\left|i\right|=\text{l}\text{o}\text{g}\left|{i}_{0}\right|-\frac{\alpha nF}{RT}\eta$$
3
where i is the current density (mA·cm− 2), i0 is the exchange current density (mA·cm− 2), α is the charge transfer coefficient in the cathode direction, ƞ is over-potential.
Based on the Eq. (3), it can be found that under a small overpotential, i and ƞ are linearly related. When the overpotential exceeds − 0.1 V, the current contribution of anode polarization is negligible. Therefore, the value of i0 can be measured by the slope of the i-ƞ curve in a narrow potential range close to the equilibrium potential.
Figure 16 shows the LSV curve on glassy carbon electrode in the bath, where when ŋ is between − 0.15 V and − 0.1 V, the polarization curve presents a straight line.
Table 2 shows the value of exchange current density i0 on glassy carbon electrode in the bath, it can be found that as the concentration of Na2MoO4 increases, the exchange current density i0 decreases; as the concentration of C6H5Na3O7 increases, the exchange current density i0 increases first and decreases then, when the concentration of C6H5Na3O7 is 0.05mol/L, i0 reaches a maximum; as the pH increases, the exchange current density i0 decreases; as the temperature increases, the exchange current density i0 increases.
Table 2
The value of exchange current density i0 on glassy carbon electrode in the bath
CNa2MoO4
(mol/L)
|
i0
(mA·cm− 2)
|
CC6H5Na3O7(mol/L)
|
i0
|
pH
|
i0
|
Temperature
(℃)
|
i0
|
0.05
|
0.0703
|
0.1
|
0.0661
|
5
|
0.1296
|
40
|
0.1975
|
0.075
|
0.0702
|
0.15
|
0.0703
|
6
|
0.0703
|
45
|
0.2306
|
0.1
|
0.0687
|
0.2
|
0.0523
|
7
|
0.0458
|
50
|
0.2413
|
0.125
|
0.0534
|
0.25
|
0.0313
|
8
|
0.0314
|
55
|
0.2452
|
0.15
|
0.0385
|
0.3
|
0.0150
|
9
|
0.0158
|
60
|
0.2458
|
3.2.3 Charge transfer impedance
Figure 17 shows Nyquist plots at -1.2 V potential in the bath. It is observed that there is only one EIS spectrum composed of a semicircular arc, which indicates that the deposition of alloy is only controlled by charge transfer[25].
According to the impedance results, Zview software was used to fit the equivalent circuit, and the result is shown as Fig. 17(e). In the circuit, Rs is the resistance of the solution, Rct is the charge transfer resistance, CPE is a constant phase element used to establish a more accurate fit.
As shown in Table 3, as the concentration of Na2MoO4 increases, the charge transfer resistance Rct increases; as the concentration of C6H5Na3O7 increases, the charge transfer resistance Rct decreases first and then increases; as the pH increases, the charge transfer resistance Rct increase; as the temperature increases, the charge transfer resistance Rct decreases.
Table 3
The value of Rs and Rct on copper electrode in the bath
CNa2MoO4
(mol/L)
|
Rct
(ohms·cm2)
|
CC6H5Na3O7
(mol/L)
|
Rct
|
pH
|
Rct
|
temperature
|
Rct
|
0.05
|
13.9000
|
0.1
|
15.4158
|
5
|
11.0002
|
40℃
|
9.6225
|
0.075
|
20.5874
|
0.15
|
13.9000
|
6
|
13.9000
|
45℃
|
8.5698
|
0.1
|
23.9291
|
0.2
|
16.7228
|
7
|
14.2071
|
50℃
|
8.4991
|
0.125
|
30.9588
|
0.25
|
16.8429
|
8
|
15.4511
|
55℃
|
8.3437
|
0.15
|
47.9219
|
0.3
|
19.2591
|
9
|
30.5490
|
60℃
|
8.0187
|