**3. Nanocrystalline Nickel-Molybdnum alloys**

Nanostructured Ni-Mo alloys functionalized with acrylic acid (AA) and dispersed in paint have shown a satisfactory performance as corrosion inhibitors which led them to be used as anticorrosive paints for petroleum industry applications [26]. Recently, few researches have been conducted to investigate the effectiveness of nanocrystalline Ni-Mo alloys as catalysts for steam reforming of hydrocarbons, such as T. Huang et al.[27] Ni-Mo bimetallic catalyst of 20.5 nm crystallite size showed high activity, superior stability and the lowest carbon deposition rate (0.00073 gc.gcat−1.h−1) in 600-h time on steam.

Moreover, owing to the nanocrystalline state of Ni-Mo alloys, a large number of active sites are provided which make these alloys perfect candidates as catalysts for hydrogen production from water electrolysis [28]. Nanocrystalline Ni-Mo alloys have been processed by different techniques such as RF magnetron sputtering, mechanical alloying and electrodeposition techniques. H. Jin-Zhao et al. [29] reported that nanocrystalline Ni-Mo alloys prepared by RF magnetron sputtering technique to be promising electrodes for hydrogen evolution reactions. While P. Kedzierzawski et al. [30] were able to produce successfully nanocrystalline Ni-Mo alloys by mechanical alloying method, as well as indicating the positive contribution of the large surface area in increasing the catalytic effect as electrodes for hydrogen production and decrease of the exchange current density.

formation of cracks, de-lamination and/or de-bonding of the different materials during thermal

In the color cathode ray tube televisions and computer monitors, the shadow mask is a perforated metal sheet which the electrons from the electron gun must pass through before reaching the phosphor screen. Its role is to ensure that the electron beam hits only the correct colored dots and does not illuminate more than the one that was intended. Only 20% of the electrons pass through the shadow mask, and the other 80% are being absorbed by the mask which leads to an increase in the temperature of the mask. The resulting thermal expansion can disturb the alignment between the apertures and the phosphor triads, leading to a distorted

The main advantages of using electrodeposited nanocrystalline over conventional Ni-Fe alloys -for the use in integrated circuit packaging or shadow masks- for cathode ray tubes include:

For soft magnetic applications, such as electromagnetic shielding, transformers materials, read-write heads, and high efficiency motors, magnetic materials- that exhibit small hysteresis losses per cycle- are required. More specifically, materials that have high permeability, low coercivity, high saturation and remnant magnetization, high electrical resistivity (to minimize

Nanostructured Ni-Mo alloys functionalized with acrylic acid (AA) and dispersed in paint have shown a satisfactory performance as corrosion inhibitors which led them to be used as anticorrosive paints for petroleum industry applications [26]. Recently, few researches have been conducted to investigate the effectiveness of nanocrystalline Ni-Mo alloys as catalysts for steam reforming of hydrocarbons, such as T. Huang et al.[27] Ni-Mo bimetallic catalyst of 20.5 nm crystallite size showed high activity, superior stability and the lowest carbon deposition

Moreover, owing to the nanocrystalline state of Ni-Mo alloys, a large number of active sites are provided which make these alloys perfect candidates as catalysts for hydrogen production

**•** Single step process to produce foils ranging in thickness from 150μm to 500μm;

**•** Finer pitch possible due to a decrease in grain size and higher strength;

**•** High etch rates due to increased grain boundary volume fraction [14].

cycles to which the components are exposed [14].

134 Modern Surface Engineering Treatments

image. This effect is known as "doming [14].

**•** High mechanical strength and hardness ( > 450VHN);

**•** Improved chemical machining performance;

*2.5.2. Magnetic applications of Ni-Fe alloys*

losses due to eddy current formation [23-25]

**3. Nanocrystalline Nickel-Molybdnum alloys**

rate (0.00073 gc.gcat−1.h−1) in 600-h time on steam.

**•** Isotropic properties due to fine equiaxed grain structure;

Furthermore, several attempts have been made in order to produce nanostructured Ni-Mo alloys by electro deposition technique to be used as cathodes for hydrogen production from water electrolysis. This is because electro deposition is considered to be cheaper than other production techniques -being mentioned previously- from the aspect of initial capital invest‐ ment and running costs [31, 32]. While it also require minor modifications to existing conven‐ tional plating lines to be able to produce nanocrystalline films or stand free objects, in addition to that scaling up is relatively easy and high production rates can also be achieved [33].

Ni-Mo deposits have been well known for their use as cathodes for hydrogen production from water by electrolysis as well as catalysts for hydrogen production by steam reforming of hydrocarbons [7]. Arul Raj and Venkatesan [34] showed an increased electrocatalytic effect of Ni-Mo electrodeposited alloys for the hydrogen evolution reaction than that showed by nickel and other nickel-based binary alloys such as Ni-Co, Ni-W, Ni-Fe, and Ni-Cr. In addition, Ni-Mo alloys are considered as highly corrosion resistant due to the good corrosion protection characteristics of molybdenum in non oxidizing solutions of hydrochloric, phosphoric, and hydrofluoric acid at most concentrations and temperatures and in boiling sulfuric acid up to about 60% concentration [35]. The nickel-molybdenum alloys normally containing 26–35wt% Mo are among the few metallic materials that are resistant to corrosion by hydrochloric acid at all concentrations and temperatures [36]. Electro deposition is one of the most promising techniques for producing nanostructure materials owing to its relative low cost compared to the other methods. Electro deposition produces nanocrystalline materials when the deposition parameters (e.g., plating bath composition, pH, temperature, current density, etc.) are opti‐ mized such that electrocrystallization results in massive nucleation and reduced grain growth [37, 38]. Due to better anticorrosive in several aggressive environments, mechanical and thermal stability characteristics of Ni-Mo alloys, the electro deposition of these alloys plays an important role. It is an example of the induced codeposition mechanism [39].

According to J. Halim et al [40], Ni-Mo nanocrystalline deposits (7–43 nm) with a nodular morphology (Figure 7) were prepared by electro deposition using direct current from citrateammonia solutions. They exhibited a single Ni-Mo solid solution phase. Increasing the applied current density led to a decrease of the molybdenum content in the deposited alloys, increase in crystallite size, and increase of the surface roughness. The highest microhardness value (285 Hv) corresponded to nanodeposits with 23% Mo. The highest corrosion resistance accompa‐ nied by relatively high hardness was detected for electrodeposits containing 15% Mo. Mo content values between 11 and 15% are recommended for obtaining better electrocatalytic activity for Hydrogen evolution reaction "HER" with the lowest cathodic Tafel's constant.

**1.** Reduction of molybdate to Mo (IV) oxide by Ni (II) species forming MoO2Ni4.

Whereas, Podlaha and Landolt [41, 42], have proposed a model based on the adsorption and catalytic reduction of molybdate species using a bath containing citrate species. This model

mediate, [Ni(II)HCit-MoO2]ads. The deposition of Mo, as indicated by this model, is only possible when Ni (II) ions are present, while nickel ions reduction following an independent

Generally, in a nickel-rich citrate electrolyte molybdenum deposition is mass-transport limited. Therefore, the Ni-Mo alloy composition is strongly influenced by the electrode rotation rate. While in a molybdenum-rich electrolyte, the rate of molybdenum deposition is limited by the flux of nickel ion. The alloy composition in this case is independent of hydrodynamic

Electro deposition parameters have a large influence on the compostion of Ni-Mo alloys, the plating current density is one of the important deposition parameters affecting the composition of Ni-Mo alloys, and it has been investigated by many researches through different plating bathes that the molybdenum content decreases as the plating current density increases E. Chassaing et al. [39], reported the decrease of molybdenum content from 30 to about 10 wt%

same conclusion has been reached in the case of Ni-Mo alloys deposited from pyrophosphate baths as indicated by M. Donten et al. [31] that Mo content ranges from 55 to 35 wt% for a

.

As for the relationship between the Mo content in the citrate bath and that in the depos‐ it, the molybdenum content in the deposit increases as the metal percentage of molybde‐ num in the bath increases [40]. The increase in the content of sodium citrate in the bath resulted in an increase of the molybdenum content of the deposit. Moreover, the molybde‐ num content in the deposit showed an increased as the pH increases till about pH = 9 and

Most of the electrodeposited Ni-Mo alloys are composed of a single phase and are mainly semi amorphous. It was found by XRD analysis that the Ni-Mo alloys electrodeposited from a citrate

With diffraction peaks being sharp at the lower content of Mo (12wt%) and wide at the high concentration of Mo (30wt%) indicating that the alloys are tending to be more amorphous as the molybdenum content increases as shown in Figure 9 [42]. A similar conclusion was made by the XRD analysis of the Ni-Mo alloys electrodeposited from pyrophosphate-ammonium-

catalyze molybdate reduction forming a surface-adsorbed inter‐

as shown in the Figure 8 [42]. The

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**2.** Reduction of the mixed oxide (MoO2Ni4) forming Ni-Mo alloy.

by increasing the current density from 10 to 150 mA/cm2

**3.2. Phase formation of nanocrystalline Ni-Mo alloys**

bath (ph 8.5-9.5) contain Ni-Mo solid solution.

plating current density from 15 to 50 mA/cm2

assumes that [Ni (II)HCit]-

path.

effects [41].

then decreased.

chloride bath (pH 8.5) [31].

**Figure 7.** SEM micrograph of Ni-Mo nanocrystalline electrodeposits [40].

#### **3.1. Mechanism of Ni-Mo electro deposition**

Ni-Mo electrodeposited alloys are considered as an example of the induced codeposition mechanism. Several hypotheses have been proposed and many investigations have been carried out to describe the Ni-Mo electro deposition mechanism. According to Chassaing et al. [39], the formation of Ni-Mo electrodeposited alloy has been explained in the following steps:


Whereas, Podlaha and Landolt [41, 42], have proposed a model based on the adsorption and catalytic reduction of molybdate species using a bath containing citrate species. This model assumes that [Ni (II)HCit] catalyze molybdate reduction forming a surface-adsorbed inter‐ mediate, [Ni(II)HCit-MoO2]ads. The deposition of Mo, as indicated by this model, is only possible when Ni (II) ions are present, while nickel ions reduction following an independent path.

Generally, in a nickel-rich citrate electrolyte molybdenum deposition is mass-transport limited. Therefore, the Ni-Mo alloy composition is strongly influenced by the electrode rotation rate. While in a molybdenum-rich electrolyte, the rate of molybdenum deposition is limited by the flux of nickel ion. The alloy composition in this case is independent of hydrodynamic effects [41].

Electro deposition parameters have a large influence on the compostion of Ni-Mo alloys, the plating current density is one of the important deposition parameters affecting the composition of Ni-Mo alloys, and it has been investigated by many researches through different plating bathes that the molybdenum content decreases as the plating current density increases E. Chassaing et al. [39], reported the decrease of molybdenum content from 30 to about 10 wt% by increasing the current density from 10 to 150 mA/cm2 as shown in the Figure 8 [42]. The same conclusion has been reached in the case of Ni-Mo alloys deposited from pyrophosphate baths as indicated by M. Donten et al. [31] that Mo content ranges from 55 to 35 wt% for a plating current density from 15 to 50 mA/cm2 .

As for the relationship between the Mo content in the citrate bath and that in the depos‐ it, the molybdenum content in the deposit increases as the metal percentage of molybde‐ num in the bath increases [40]. The increase in the content of sodium citrate in the bath resulted in an increase of the molybdenum content of the deposit. Moreover, the molybde‐ num content in the deposit showed an increased as the pH increases till about pH = 9 and then decreased.

#### **3.2. Phase formation of nanocrystalline Ni-Mo alloys**

**Figure 7.** SEM micrograph of Ni-Mo nanocrystalline electrodeposits [40].

Ni-Mo electrodeposited alloys are considered as an example of the induced codeposition mechanism. Several hypotheses have been proposed and many investigations have been carried out to describe the Ni-Mo electro deposition mechanism. According to Chassaing et al. [39], the formation of Ni-Mo electrodeposited alloy has been explained in the following

**3.1. Mechanism of Ni-Mo electro deposition**

136 Modern Surface Engineering Treatments

steps:

Most of the electrodeposited Ni-Mo alloys are composed of a single phase and are mainly semi amorphous. It was found by XRD analysis that the Ni-Mo alloys electrodeposited from a citrate bath (ph 8.5-9.5) contain Ni-Mo solid solution.

With diffraction peaks being sharp at the lower content of Mo (12wt%) and wide at the high concentration of Mo (30wt%) indicating that the alloys are tending to be more amorphous as the molybdenum content increases as shown in Figure 9 [42]. A similar conclusion was made by the XRD analysis of the Ni-Mo alloys electrodeposited from pyrophosphate-ammoniumchloride bath (pH 8.5) [31].

**3.3. Properties of nanocrystalline Ni-Mo alloys**

*3.3.1. Corrosion properties of nanocrystalline Ni-Mo alloys*

and decreased when the Mo content in these alloys is increased [43].

Corrosion resistance of nanocrystalline materials is of a great importance in assessing a wide range of potential future applications. To date, a few researches have addressed this issue. Ni-Mo alloys have been studied for their corrosion resistance especially in the media where they are used as cathodes for hydrogen evolution [34]. As indicated previously, Ni-Mo alloys are of excellent corrosion resistance especially in the aqueous solutions contain‐ ing chloride ions [31]. As for Ni-Mo nanocrystalline alloys, they showed promising protective characteristics evidenced by polarization resistance of about 3.5-17 kΩ. While polarization curves being obtained for Ni-Mo nanocrystalline alloys being immersed in 0.5 M NaCl for various periods as shown in Figure 10 and 11, indicated that at the begin‐ ning the alloy with higher Mo content (27-30wt%) having a less negative potential (-0.014V) vs. Ag/AgCl than that for the alloy containing lower Mo content (13-15 wt%) recording a potential of about -0.749V vs. Ag/AgCl. As the immersion period increased, the corrosion potential moved towards more electronegative values, down to about -0.93 V vs. Ag/ AgCl, regardless the alloy composition [43]. While in the deaerated hydrochloric solu‐ tions, nanocrystalline Ni-Mo alloys being deposited from citrate solution (pH 8.5-9.5) show a large passivation domain without any pitting. The corrosion currents as well as the passivation currents were higher than for the bulk conventional Ni-Mo alloy (Hastelloy B)

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**Figure 10.** Polarization curves in semilogarithmic coordinates for Ni-Mo alloy (27-30% Mo) deposit in 0.5 M NaCl for

various periods of continuous immersion (25 °C, 5 mV/s; geometrical surface of WE-0.63585 cm2) [43].

**Figure 8.** Molybdenum content as a function of the applied current density. Curve 1: 0.02 M Na2MoO4, pH 8.5; Curve 2: 0.02 M Na2MoO4, pH 9.5; Curve 3: 0.03M Na2MoO4 pH 9.5 [42].

**Figure 9.** XRD patterns for Ni–Mo layers deposited from solution containing 0.03 M Na2MoO4 at pH 9.5 [42].

#### **3.3. Properties of nanocrystalline Ni-Mo alloys**

**Figure 8.** Molybdenum content as a function of the applied current density. Curve 1: 0.02 M Na2MoO4, pH 8.5; Curve

**Figure 9.** XRD patterns for Ni–Mo layers deposited from solution containing 0.03 M Na2MoO4 at pH 9.5 [42].

2: 0.02 M Na2MoO4, pH 9.5; Curve 3: 0.03M Na2MoO4 pH 9.5 [42].

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#### *3.3.1. Corrosion properties of nanocrystalline Ni-Mo alloys*

Corrosion resistance of nanocrystalline materials is of a great importance in assessing a wide range of potential future applications. To date, a few researches have addressed this issue. Ni-Mo alloys have been studied for their corrosion resistance especially in the media where they are used as cathodes for hydrogen evolution [34]. As indicated previously, Ni-Mo alloys are of excellent corrosion resistance especially in the aqueous solutions contain‐ ing chloride ions [31]. As for Ni-Mo nanocrystalline alloys, they showed promising protective characteristics evidenced by polarization resistance of about 3.5-17 kΩ. While polarization curves being obtained for Ni-Mo nanocrystalline alloys being immersed in 0.5 M NaCl for various periods as shown in Figure 10 and 11, indicated that at the begin‐ ning the alloy with higher Mo content (27-30wt%) having a less negative potential (-0.014V) vs. Ag/AgCl than that for the alloy containing lower Mo content (13-15 wt%) recording a potential of about -0.749V vs. Ag/AgCl. As the immersion period increased, the corrosion potential moved towards more electronegative values, down to about -0.93 V vs. Ag/ AgCl, regardless the alloy composition [43]. While in the deaerated hydrochloric solu‐ tions, nanocrystalline Ni-Mo alloys being deposited from citrate solution (pH 8.5-9.5) show a large passivation domain without any pitting. The corrosion currents as well as the passivation currents were higher than for the bulk conventional Ni-Mo alloy (Hastelloy B) and decreased when the Mo content in these alloys is increased [43].

**Figure 10.** Polarization curves in semilogarithmic coordinates for Ni-Mo alloy (27-30% Mo) deposit in 0.5 M NaCl for various periods of continuous immersion (25 °C, 5 mV/s; geometrical surface of WE-0.63585 cm2) [43].

composite components. All these modifications aimed at obtaining the electrodes with very developed, rough or porous electrode surface. Many types of particles were used to improve mechanical, physicochemical or electrocatalytic properties of composite coatings, like car‐ bides, silicides, nitrides, and oxides [47, 48]. Recent research in electro deposition suggested a technique involving codeposition of metallic particles to form electrodeposited metal matrix/ metal particle composites [49]. Among these composites are those containing metals like Al, Ti, V, Mo which could not be directly deposited from aqueous solutions. Incorporating such powdered components to the metal matrix leads to obtain a new kind of composite material which could be applied as electrode materials [50- 53]. Ni-based binary composite coatings like Ni–Mo, Ni–Zn, Ni–Co, Ni–W, Ni–Fe and Ni–Cr were tried for hydrogen electrodes; out of these electrodes, Ni–Mo was found to be best and most stable electrode with an overpotential of 0.18 V in 6 M KOH solutions [54]. Also according to Kubisztal et al. [55] electrolytic Ni–Mo and Ni–Mo–Si coatings were prepared by codeposition of nickel with silicon and molybdenum powders from a nickel bath in which Mo and Si particles were suspended by stirring. Com‐ posite coatings are characterized by very porous surface in comparison with nickel coating after the same thermal treatment. Ni–Mo composite coatings, obtained by electrodeposition of Ni with Mo particles on a steel substrate from the nickel bath containing suspended Mo powder, showed pronounced improvement in the electrochemical performance for HER in an alkaline environment compared to nickel electrode [47, 55]. The molybdenum content and the thickness of the Ni–Mo composite coatings change between 28–46 wt%, and 100–130 nm, respectively depending on the deposition current density. Ni–Mo electrodeposits were characterized by larger surface than the Ni electrodeposits. According to Jovic et al. [56], improved performances are to be expected if a composite compact layer of Ni and some Mo oxides could be prepared by the simultaneous electrodeposition of Ni and MoO3 from an electrolyte solution in which MoO3 particles are suspended. It seems a unique way for solving the problem of porosity of electroplated Ni–Mo coatings and low mechanical stability of

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Ni–Mo nanocomposite coatings (18–32 nm) were prepared by electrodeposition of nickel from a nickel salt bath containing suspended Mo nanoparticles (Figure 12), by Abdel-Karim et al [57]. All the coatings have been deposited under galvanostatic conditions using current

diffraction, the obtained coatings consisted of crystalline Mo phase incorporated into Ni matrix (Figure13). The molybdenum content diminished with increasing the deposition current density and ranged between ∼6 and ∼17% Mo. Table 4 summarizes the corrosion properties of Ni-Mo composites examined in a remarkable deterioration in the corrosion resistance of Ni– Mo composites was observed with the increase of Mo content due to crystallite size-refining and surface roughness effect. Electrocatalytic effect for hydrogen production was improved mainly as a result of increasing the surface roughness and thus providing more accessible

According to Low and Walsh [58], many operating parameters influence the quantity of incorporated particles, including current density, bath agitation and electrolyte composi‐ tion. It has been suggested that the transport of particles is due to electrophoresis,

. According to structural investigation carried out by X-ray

thermally prepared Ni–Mo catalysts.

densities in the range 5–80 mA/cm2

surface area.

**Figure 11.** Polarization curves in semilogarithmic coordinates for Ni-Mo alloy (13-15% Mo) deposit in 0.5 M NaCl for various periods of continuous immersion (25 °C, 5 mV/s; geometrical surface of WE-0.63585 cm2) [43].

#### *3.3.2. Electrocatalytic reactivity for hydrogen evolution*

Nanocrystalline Ni-Mo alloys are known for their premium electrocatalytic properties as the presence of molybdenum in these materials apparently increases their catalytic activity. Ni-Mo alloy coatings electrodeosited from pyrophosphate-sodium bicarbonate bath possess high catalytic activity for hydrogen evolution in the NaOH solutions. Their stability in the 1 M NaOH at 25°C under the condition of the reverse polarization are of much better activity toward hydrogen evolution reaction than pure Ni electrode as the overpotential for Ni-Mo electrodeposited alloys was recorded as -1.3V vs. SCE at j = -0.3 Acm-2 compared to -1.66 V vs.SCE for Ni electrode [44, 45].

#### **4. Electrodeposition of Ni-Mo nano composites**

Broad application of nickel-based composite coatings in electrochemistry is due to the highly catalytic activity in electrocatalytic hydrogen evolution (HER) and electrocatalytic oxygen evolution (OER) as well as good corrosion resistance of nickel in aggressive environments [46]. In order to improve the properties of these materials, and enhance their catalytic activity, various modifications could be applied, such as alloying with other elements, incorporating composite components. All these modifications aimed at obtaining the electrodes with very developed, rough or porous electrode surface. Many types of particles were used to improve mechanical, physicochemical or electrocatalytic properties of composite coatings, like car‐ bides, silicides, nitrides, and oxides [47, 48]. Recent research in electro deposition suggested a technique involving codeposition of metallic particles to form electrodeposited metal matrix/ metal particle composites [49]. Among these composites are those containing metals like Al, Ti, V, Mo which could not be directly deposited from aqueous solutions. Incorporating such powdered components to the metal matrix leads to obtain a new kind of composite material which could be applied as electrode materials [50- 53]. Ni-based binary composite coatings like Ni–Mo, Ni–Zn, Ni–Co, Ni–W, Ni–Fe and Ni–Cr were tried for hydrogen electrodes; out of these electrodes, Ni–Mo was found to be best and most stable electrode with an overpotential of 0.18 V in 6 M KOH solutions [54]. Also according to Kubisztal et al. [55] electrolytic Ni–Mo and Ni–Mo–Si coatings were prepared by codeposition of nickel with silicon and molybdenum powders from a nickel bath in which Mo and Si particles were suspended by stirring. Com‐ posite coatings are characterized by very porous surface in comparison with nickel coating after the same thermal treatment. Ni–Mo composite coatings, obtained by electrodeposition of Ni with Mo particles on a steel substrate from the nickel bath containing suspended Mo powder, showed pronounced improvement in the electrochemical performance for HER in an alkaline environment compared to nickel electrode [47, 55]. The molybdenum content and the thickness of the Ni–Mo composite coatings change between 28–46 wt%, and 100–130 nm, respectively depending on the deposition current density. Ni–Mo electrodeposits were characterized by larger surface than the Ni electrodeposits. According to Jovic et al. [56], improved performances are to be expected if a composite compact layer of Ni and some Mo oxides could be prepared by the simultaneous electrodeposition of Ni and MoO3 from an electrolyte solution in which MoO3 particles are suspended. It seems a unique way for solving the problem of porosity of electroplated Ni–Mo coatings and low mechanical stability of thermally prepared Ni–Mo catalysts.

**Figure 11.** Polarization curves in semilogarithmic coordinates for Ni-Mo alloy (13-15% Mo) deposit in 0.5 M NaCl for

Nanocrystalline Ni-Mo alloys are known for their premium electrocatalytic properties as the presence of molybdenum in these materials apparently increases their catalytic activity. Ni-Mo alloy coatings electrodeosited from pyrophosphate-sodium bicarbonate bath possess high catalytic activity for hydrogen evolution in the NaOH solutions. Their stability in the 1 M NaOH at 25°C under the condition of the reverse polarization are of much better activity toward hydrogen evolution reaction than pure Ni electrode as the overpotential for Ni-Mo electrodeposited alloys was recorded as -1.3V vs. SCE at j = -0.3 Acm-2 compared to -1.66 V

Broad application of nickel-based composite coatings in electrochemistry is due to the highly catalytic activity in electrocatalytic hydrogen evolution (HER) and electrocatalytic oxygen evolution (OER) as well as good corrosion resistance of nickel in aggressive environments [46]. In order to improve the properties of these materials, and enhance their catalytic activity, various modifications could be applied, such as alloying with other elements, incorporating

various periods of continuous immersion (25 °C, 5 mV/s; geometrical surface of WE-0.63585 cm2) [43].

*3.3.2. Electrocatalytic reactivity for hydrogen evolution*

**4. Electrodeposition of Ni-Mo nano composites**

vs.SCE for Ni electrode [44, 45].

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Ni–Mo nanocomposite coatings (18–32 nm) were prepared by electrodeposition of nickel from a nickel salt bath containing suspended Mo nanoparticles (Figure 12), by Abdel-Karim et al [57]. All the coatings have been deposited under galvanostatic conditions using current densities in the range 5–80 mA/cm2 . According to structural investigation carried out by X-ray diffraction, the obtained coatings consisted of crystalline Mo phase incorporated into Ni matrix (Figure13). The molybdenum content diminished with increasing the deposition current density and ranged between ∼6 and ∼17% Mo. Table 4 summarizes the corrosion properties of Ni-Mo composites examined in a remarkable deterioration in the corrosion resistance of Ni– Mo composites was observed with the increase of Mo content due to crystallite size-refining and surface roughness effect. Electrocatalytic effect for hydrogen production was improved mainly as a result of increasing the surface roughness and thus providing more accessible surface area.

According to Low and Walsh [58], many operating parameters influence the quantity of incorporated particles, including current density, bath agitation and electrolyte composi‐ tion. It has been suggested that the transport of particles is due to electrophoresis, mechanical entrapment, adsorption, and convection–diffusion. The current density has been found to influence the amount of alumina nanoparticles incorporated into electrode‐ posited nickel. An increase in current density resulted in a rough surface microstructure and lead to less Al2O3 nanoparticles being incorporated in the metal deposit. The trend of decreasing the molybdenum content in Ni–Mo composites as a result of raising the applied current density has been also reported by Kubisztal et al. [55]. This phenomenon could be due to the fact that the amount of Mo powder incorporated in the composite depends on the rate of mass transport. At lower current densities Mo powder has longer time to reach the Ni matrix and form Ni–Mo composite. Whereas, at higher current densities, the Ni layers grow faster and less time is allowed for Mo powder to be transferred to the Ni matrix [54]. Another explanation for the same phenomenon is that by increasing the current density, a strong electric field is produced which in turn creates a partial desorption of nickel ions on the surface of Mo particles [59, 60]. The Ni crystallite size was reduced from ∼32 to ∼18 nm as the current density was decreased from 80 to 5 mA/cm<sup>2</sup> . These values are less than that for Ni crystallites (62 nm) reported by Panek and Budniok [59]. This fact could be explained by the incorporation of metallic powder particles into the nickel matrix and the influence of the deposition current density. When electrically conductive parti‐ cles are embedded into the coating, they effectively become a part of the cathode and act as nucleation sites for the Ni matrix. A structure refinement occurs relative to pure Ni coatings due to the periodic nucleation and growth from the surface of the particles.

The generally accepted mechanism of the HER in alkaline solution is based on the following steps:

$$\rm{M} + \rm{H}\_{2}\rm{O} + \rm{e} \rightarrow \rm{MH}\_{ads} + \rm{OH}^{\cdot} \tag{6}$$

**Figure 12.** SEM micrographs for electrodeposited layers of Ni–Mo composites [57].

**Figure 13.** XRD of electrodeposited Ni-Mo nanocomposites [57].

**4.1. Corrosion properties of electrodeposited Ni–Mo composites**

From Table 4, electrodeposited Ni–Mo composites prepared by R. Abdel-karim et al et al [57] showed higher corrosion rates (0.035–1.795 mm/y) compared to the corrosion rates of Ni–Mo electrodeposited alloys (4.7–8.3 ×10−3 mm/y) [9]. This result would be attributed to the nonhomogeneity and the rough surface of the Ni–Mo composites compared to the surface of Ni– Mo alloys. The highest electrocatalytic activity is detected for Ni–Mo composite containing

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$$\text{CHH}\_{\text{ads}} + \text{H}\_2\text{O} + \text{e} \rightarrow \text{H}2 + \text{M} + \text{OH}^-\tag{7}$$

$$2\text{ MH} \rightarrow \text{ H}\_2 + 2\text{ M} \tag{8}$$

where (1) is the proton discharge electrosorption (Volmer reaction), which is followed by electrodesorption step (2) (Heyrovsky reaction) and/or H recombination step (3) (Tafel reaction). According to general models for HER mechanisms, the Volmer–Heyrovsky and Tafel reaction mechanism, reactions (1)–(3), may display three different slopes: 116.3, 38.8 or 29.1 mV dec−1 at 20 °C. When Heyrovsky reaction is the rate determining step, r.d.s., the slope is 38.8 mV dec−1 and when the Tafel reaction is the r.d.s. slope is 29.1 mV dec−1. When the slope of 116.3 mV dec−1 is observed, it is impossible to distinguish which step is the rate determining one. However, as the surface coverage by adsorbed hydrogen should increase with the increase in negative overpotential, the rate limiting step should be that of Heyrovsky [54, 60].

**Figure 12.** SEM micrographs for electrodeposited layers of Ni–Mo composites [57].

mechanical entrapment, adsorption, and convection–diffusion. The current density has been found to influence the amount of alumina nanoparticles incorporated into electrode‐ posited nickel. An increase in current density resulted in a rough surface microstructure and lead to less Al2O3 nanoparticles being incorporated in the metal deposit. The trend of decreasing the molybdenum content in Ni–Mo composites as a result of raising the applied current density has been also reported by Kubisztal et al. [55]. This phenomenon could be due to the fact that the amount of Mo powder incorporated in the composite depends on the rate of mass transport. At lower current densities Mo powder has longer time to reach the Ni matrix and form Ni–Mo composite. Whereas, at higher current densities, the Ni layers grow faster and less time is allowed for Mo powder to be transferred to the Ni matrix [54]. Another explanation for the same phenomenon is that by increasing the current density, a strong electric field is produced which in turn creates a partial desorption of nickel ions on the surface of Mo particles [59, 60]. The Ni crystallite size was reduced from

∼32 to ∼18 nm as the current density was decreased from 80 to 5 mA/cm<sup>2</sup>

steps:

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are less than that for Ni crystallites (62 nm) reported by Panek and Budniok [59]. This fact could be explained by the incorporation of metallic powder particles into the nickel matrix and the influence of the deposition current density. When electrically conductive parti‐ cles are embedded into the coating, they effectively become a part of the cathode and act as nucleation sites for the Ni matrix. A structure refinement occurs relative to pure Ni coatings due to the periodic nucleation and growth from the surface of the particles.

The generally accepted mechanism of the HER in alkaline solution is based on the following

where (1) is the proton discharge electrosorption (Volmer reaction), which is followed by electrodesorption step (2) (Heyrovsky reaction) and/or H recombination step (3) (Tafel reaction). According to general models for HER mechanisms, the Volmer–Heyrovsky and Tafel reaction mechanism, reactions (1)–(3), may display three different slopes: 116.3, 38.8 or 29.1 mV dec−1 at 20 °C. When Heyrovsky reaction is the rate determining step, r.d.s., the slope is 38.8 mV dec−1 and when the Tafel reaction is the r.d.s. slope is 29.1 mV dec−1. When the slope of 116.3 mV dec−1 is observed, it is impossible to distinguish which step is the rate determining one. However, as the surface coverage by adsorbed hydrogen should increase with the increase

in negative overpotential, the rate limiting step should be that of Heyrovsky [54, 60].



<sup>2</sup> 2 MH H + 2 M ® (8)

. These values

**Figure 13.** XRD of electrodeposited Ni-Mo nanocomposites [57].

#### **4.1. Corrosion properties of electrodeposited Ni–Mo composites**

From Table 4, electrodeposited Ni–Mo composites prepared by R. Abdel-karim et al et al [57] showed higher corrosion rates (0.035–1.795 mm/y) compared to the corrosion rates of Ni–Mo electrodeposited alloys (4.7–8.3 ×10−3 mm/y) [9]. This result would be attributed to the nonhomogeneity and the rough surface of the Ni–Mo composites compared to the surface of Ni– Mo alloys. The highest electrocatalytic activity is detected for Ni–Mo composite containing ∼6% Mo as well as the high surface roughness value (5.35 μm). The obtained results are in agreement with the results obtained by Panek and Budniok [59] and would indicate that both factors (Mo content and surface roughness) influence the electrocatlaytic behavior of Ni–Mo composites. The decrease of one of these two factors would lead to reduction in the electroca‐ talytic activity as for hydrogen evolution reaction. According to Kubisztal et al. [55], the main contribution toward the electrocatalytic activity of Ni–Mo composites is attributed to the increase in the actual surface area due to higher surface roughness. Mo particles, while embedded in the Ni matrix, produce a moderate increase in the catalytic effect in the point of contact.

The advantages of using the AAO membrane as a template are firstly, that it allows the diameter of the nanowires, nanorods and nanotube to be tailored to the respective pore size in the membrane (Figure 14) [63]. Secondly, it ensures that the growth of the nanocrystal (nanowire, nanorod, nanotube) is aligned within the high aspect ratio nano-channel which is also perpendicular to the substrate surface at the base of the membrane. A wide variety of materials that include metals, oxides, conductive polymers and semiconductors can then be deposited into the pores of the membrane. Then a suitable formation mechanism can be used to generate nanowires, nanorods (short nanowires) and nanotubes. The dimensions of which can be controlled by adjusting the template pore geometry and the formation parameters [64].

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**Figure 14.** Template Assisted Growth of Nanowires and Nanorods [63]

produce a variety of metal nanowires [66].

Electrodeposition of nanoscale materials in the pores of a self- ordered nanochannel matrix is of relatively low cost. Furthermore, electrodeposition is a fast process for the fabrication of large arrays of nanostructures with a very large aspect ratio, which is not possible with standard lithographic techniques [65]. Electrochemical synthesis in a template is taken as one of the most efficient methods in controlling the growth of nanowires and has been used to

Compared to previous work [40] and from table 5 [57], the Ni–Mo composite offers a higher electrochemical activity toward hydrogen evolution reaction (HER) than that of Ni–Mo alloys, with the sample containing 17% Mo had the lowest overpotential (−0.725 mV) at j = −1.5 mA/ cm<sup>2</sup> . These observations are in agreement with Popczyk [60].



**Table 4.** Corrosion properties of electrodeposited Ni-Mo nanocrystalline composites

**Table 5.** Electrocatalyric properties of electrodeposited Ni-Mo nanocrystalline composites

### **5. Nano-porous alumina formation**

Nanoporous alumina films "AAO" produced during electrochemical anodization of alumi‐ num has been studied for many years, and has continued to attract interest from various researchers because of its unique chemical and physical properties. These unique properties have made it possible for a wider application such as electronic devices, magnetic storage disks, sensors in hydrogen detection, adsorption of volatile organic compounds; biodevices; and in drug delivery, etc [61- 63].

The advantages of using the AAO membrane as a template are firstly, that it allows the diameter of the nanowires, nanorods and nanotube to be tailored to the respective pore size in the membrane (Figure 14) [63]. Secondly, it ensures that the growth of the nanocrystal (nanowire, nanorod, nanotube) is aligned within the high aspect ratio nano-channel which is also perpendicular to the substrate surface at the base of the membrane. A wide variety of materials that include metals, oxides, conductive polymers and semiconductors can then be deposited into the pores of the membrane. Then a suitable formation mechanism can be used to generate nanowires, nanorods (short nanowires) and nanotubes. The dimensions of which can be controlled by adjusting the template pore geometry and the formation parameters [64].

∼6% Mo as well as the high surface roughness value (5.35 μm). The obtained results are in agreement with the results obtained by Panek and Budniok [59] and would indicate that both factors (Mo content and surface roughness) influence the electrocatlaytic behavior of Ni–Mo composites. The decrease of one of these two factors would lead to reduction in the electroca‐ talytic activity as for hydrogen evolution reaction. According to Kubisztal et al. [55], the main contribution toward the electrocatalytic activity of Ni–Mo composites is attributed to the increase in the actual surface area due to higher surface roughness. Mo particles, while embedded in the Ni matrix, produce a moderate increase in the catalytic effect in the point of

Compared to previous work [40] and from table 5 [57], the Ni–Mo composite offers a higher electrochemical activity toward hydrogen evolution reaction (HER) than that of Ni–Mo alloys, with the sample containing 17% Mo had the lowest overpotential (−0.725 mV) at j = −1.5 mA/

**mA/cm2 Mo content, %wt Ecorr, mV Icorr, μm/cm<sup>2</sup> Corrosion rate,**


> **Ni crystallite size, nm**

> > 18.3 25.6 28.5 32.1

42.7 153.5 105.6 2.94

**Cathodic mV/decade**

> -115.2 -142.7 -118 -34.9

**mm/y**

0.5 1.795 1.236 0.035

**Evs SCE(V) at j= -1.5 mA/cm2**

> -1 -0.725 -0.92 n.a

. These observations are in agreement with Popczyk [60].

14.6 17.22 16.7 6.4

**Table 4.** Corrosion properties of electrodeposited Ni-Mo nanocrystalline composites

**Roughness, Rq, μm**

> 0.965 25.6 28.5 32.1

Nanoporous alumina films "AAO" produced during electrochemical anodization of alumi‐ num has been studied for many years, and has continued to attract interest from various researchers because of its unique chemical and physical properties. These unique properties have made it possible for a wider application such as electronic devices, magnetic storage disks, sensors in hydrogen detection, adsorption of volatile organic compounds; biodevices; and in

**Table 5.** Electrocatalyric properties of electrodeposited Ni-Mo nanocrystalline composites

**Mo content, %wt**

> 14.6 17.2 16.7 6.35

**5. Nano-porous alumina formation**

drug delivery, etc [61- 63].

contact.

cm<sup>2</sup>

**Plating current density,**

144 Modern Surface Engineering Treatments

**Plating current density, mA/cm2**

**Figure 14.** Template Assisted Growth of Nanowires and Nanorods [63]

Electrodeposition of nanoscale materials in the pores of a self- ordered nanochannel matrix is of relatively low cost. Furthermore, electrodeposition is a fast process for the fabrication of large arrays of nanostructures with a very large aspect ratio, which is not possible with standard lithographic techniques [65]. Electrochemical synthesis in a template is taken as one of the most efficient methods in controlling the growth of nanowires and has been used to produce a variety of metal nanowires [66].

AAO template is an ideal mold because it possesses many desirable characteristics, including tunable pore dimensions, good mechanical property, and good thermal stability. Moreover, especially for metal nanowires, the AAO template has been proved to be a cheap and high yield technique to produce large arrays of metals nanowires by the electrodeposition. This oxide has ordered hexagonal cells, of which every cell contains a cylindrical pore at its center. The pore diameter, cell size and barrier layer thickness can be controlled by anodizing voltage and the depth of pore by anodizing time [61]. Masuda et al. [64] has shown that AAO mem‐ branes with large pore sizes can be used in optical devices, particularly in the infra-red region of the spectrum.

electrical field and the second is the dissolution of the forming oxide layer. In addition, if there are regions of high current flows when the electric field is applied, an increased dissolution

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The origin of pore nuclei and the exact mechanism of pore nucleation are still largely unknown. Several formation models have been proposed [76, 77]; one model explains that pore nucleation results from an electric field assisted local chemical dissolution [78] at the electrolyte/oxide interface and oxide generation at the metal/oxide interface. For electrolytes with a pH less than 5, there is a significant flow of Al3+ ions into the electrolyte and as a consequence there are regions where the formation of new oxide at the oxide/electrolyte interface is unstable. This regional instability produces variations in the applied electrical field; this in turn results in an increased dissolution rate [78, 79]. This mechanism produces an underlying metal/oxide and oxide/electrolyte interfaces that consist of a large numbers of hemispherical depressions per cm2 that corresponds to the pores density. In these depressions the electrical field tends to be more concentrated due to the focusing effect of the hemispherical shape, hence the increased dissolution rate. [80]. In contrast, the electrical field is fairly constant over the surface of the barrier layer formed in an electrolyte with a pH greater than 5, where the oxide thickness is uniform and stable. These hemispherical depressions form the foundations of the resulting pore structures. The location of these depressions is also influenced by the initial surface topography, surface imperfections such as impurities, pits, scratches, grain boundaries and surface treatments prior to anodization [81]. Patermarakis et al. [82] proposed a pore nucleation model that results from the spontaneous recrystallization of the unstable rare lattice of oxide formed at the surface of the Al adjacent to metal/oxide interface to a more stable denser nanocrystalline oxide located in the oxide layer. The resulting recrystallization ruptures in the surface and produces regions of rarefied oxide between nanocrystallites (anhydrous/amor‐ phous). It is in these regions that pore nuclei form. Earlier studies by Habazaki et al. [77] indicated the potential for the enrichment of alloying elements, dopants and/or impurities in the Al substrate adjacent to the metal/oxide interface. The enrichment layers were found to be about 1 to 5 nm thick immediately beneath the metal/oxide interface and were a consequence of the oxide growth. These enrichment layers may also be involved in the initiation of changes within the oxide layer that promote pore nucleation. In a recent investigation by Zaraska et al. [78], the presence of alloying elements in an Al alloy (AA1050) not only slowed the rate of oxide growth but also influenced structural features such as porosity, barrier layer thickness,

rate can result (field assisted dissolution) [75].

pore diameter and pore density of the forming oxide layer.

that forms the pore bottom, as shown in Figure 15 [75].

In the early stages of the anodization process Al3+ ions migrate from the metal across the metal/ oxide interface into the forming oxide layer [83]. Meanwhile O2- ions formed from water at the oxide/electrolyte interface travel into the oxide layer. During this stage approximately 70% of the Al3+ ions and the O2- ions contribute to the formation of the barrier oxide layer [79], the remaining Al3+ ions are dissolved into the electrolyte. This condition has been shown to be the prerequisite for porous oxide growth, in which the Al-O bonds in the oxide lattice break to release Al3+ ions [80]. During the oxide formation the barrier layer constantly regenerates with further oxide growth and transforms into a semi-spherical oxide layer of constant thickness

The controlled placement of nano-dots on a substrate can be achieved with great accuracy using electron beam lithography. The major disadvantages of using this technique are the high capital cost of the equipment and the long exposure times which result in a low production output. An alternative process for the large scale fabrication of nano-dots on a semiconductor substrate uses an AAO membrane as an evaporation mask. The membrane provides an array of uniformly sized pores and site controlled pore locations where the nano-dots can be deposited. Before being used as a mask, the barrier layer is removed from the AAO membrane using a suitable etching technique, leaving a through pore structure or nano-channel. The major advantage of manufacturing nano-dot arrays using an AAO membrane is that the membrane can be used as a template. The template provides the precise location of individual pores in a high-density pore array without the need for expensive lithographic processes. The potential technological application of nano-dots is in the fabrication of ultra-small electronic devices, ultrahigh-density recording media, and nano-catalysis applications [64].

#### **5.1. Nano-porous alumina formation mechanism**

The formation process of the nano-porous oxide layer is a complex process that produces a self- organized hexagonal pore array, these hexagonal honeycomb structures have been reported by several researchers [67-73]. The porous structure consists of a thin non porous oxide layer of constant thickness that is adjacent to the metal substrate that continually regenerates at the base of the pore while the pore wall is being created, this wall increases in height with time. The particular electrolyte, its concentration, the anodic voltage and bath temperature are the main parameters in determining the pore size and the distance between pores [74].

Typical electrolytes used to produce this type of oxide layer have a pH that is less than 5, and slowly dissolve the forming oxide layer. Examples of the acids used are sulfuric, phosphoric and oxalic. However; mixtures of organic and inorganic acids have also been used. The properties of the electrolyte are important in the formation of porosity and permeability. Electrolytes that are composed of less concentrated acids tend to produces oxide coatings that are harder, thicker, less porous and more wear resistant than those composed of higher concentrated acids. But the most important factor that must be considered when forming the porous oxide is the electrolyte's ability to sustain a significant flow of Al3+ ions from the metal substrate into the electrolyte. There are two mechanisms that are responsible for the loss of Al3+ ions from the metal substrate. The first is by the direct expulsion of ions by the applied electrical field and the second is the dissolution of the forming oxide layer. In addition, if there are regions of high current flows when the electric field is applied, an increased dissolution rate can result (field assisted dissolution) [75].

AAO template is an ideal mold because it possesses many desirable characteristics, including tunable pore dimensions, good mechanical property, and good thermal stability. Moreover, especially for metal nanowires, the AAO template has been proved to be a cheap and high yield technique to produce large arrays of metals nanowires by the electrodeposition. This oxide has ordered hexagonal cells, of which every cell contains a cylindrical pore at its center. The pore diameter, cell size and barrier layer thickness can be controlled by anodizing voltage and the depth of pore by anodizing time [61]. Masuda et al. [64] has shown that AAO mem‐ branes with large pore sizes can be used in optical devices, particularly in the infra-red region

The controlled placement of nano-dots on a substrate can be achieved with great accuracy using electron beam lithography. The major disadvantages of using this technique are the high capital cost of the equipment and the long exposure times which result in a low production output. An alternative process for the large scale fabrication of nano-dots on a semiconductor substrate uses an AAO membrane as an evaporation mask. The membrane provides an array of uniformly sized pores and site controlled pore locations where the nano-dots can be deposited. Before being used as a mask, the barrier layer is removed from the AAO membrane using a suitable etching technique, leaving a through pore structure or nano-channel. The major advantage of manufacturing nano-dot arrays using an AAO membrane is that the membrane can be used as a template. The template provides the precise location of individual pores in a high-density pore array without the need for expensive lithographic processes. The potential technological application of nano-dots is in the fabrication of ultra-small electronic

devices, ultrahigh-density recording media, and nano-catalysis applications [64].

The formation process of the nano-porous oxide layer is a complex process that produces a self- organized hexagonal pore array, these hexagonal honeycomb structures have been reported by several researchers [67-73]. The porous structure consists of a thin non porous oxide layer of constant thickness that is adjacent to the metal substrate that continually regenerates at the base of the pore while the pore wall is being created, this wall increases in height with time. The particular electrolyte, its concentration, the anodic voltage and bath temperature are the main parameters in determining the pore size and the distance between

Typical electrolytes used to produce this type of oxide layer have a pH that is less than 5, and slowly dissolve the forming oxide layer. Examples of the acids used are sulfuric, phosphoric and oxalic. However; mixtures of organic and inorganic acids have also been used. The properties of the electrolyte are important in the formation of porosity and permeability. Electrolytes that are composed of less concentrated acids tend to produces oxide coatings that are harder, thicker, less porous and more wear resistant than those composed of higher concentrated acids. But the most important factor that must be considered when forming the porous oxide is the electrolyte's ability to sustain a significant flow of Al3+ ions from the metal substrate into the electrolyte. There are two mechanisms that are responsible for the loss of Al3+ ions from the metal substrate. The first is by the direct expulsion of ions by the applied

**5.1. Nano-porous alumina formation mechanism**

of the spectrum.

146 Modern Surface Engineering Treatments

pores [74].

The origin of pore nuclei and the exact mechanism of pore nucleation are still largely unknown. Several formation models have been proposed [76, 77]; one model explains that pore nucleation results from an electric field assisted local chemical dissolution [78] at the electrolyte/oxide interface and oxide generation at the metal/oxide interface. For electrolytes with a pH less than 5, there is a significant flow of Al3+ ions into the electrolyte and as a consequence there are regions where the formation of new oxide at the oxide/electrolyte interface is unstable. This regional instability produces variations in the applied electrical field; this in turn results in an increased dissolution rate [78, 79]. This mechanism produces an underlying metal/oxide and oxide/electrolyte interfaces that consist of a large numbers of hemispherical depressions per cm2 that corresponds to the pores density. In these depressions the electrical field tends to be more concentrated due to the focusing effect of the hemispherical shape, hence the increased dissolution rate. [80]. In contrast, the electrical field is fairly constant over the surface of the barrier layer formed in an electrolyte with a pH greater than 5, where the oxide thickness is uniform and stable. These hemispherical depressions form the foundations of the resulting pore structures. The location of these depressions is also influenced by the initial surface topography, surface imperfections such as impurities, pits, scratches, grain boundaries and surface treatments prior to anodization [81]. Patermarakis et al. [82] proposed a pore nucleation model that results from the spontaneous recrystallization of the unstable rare lattice of oxide formed at the surface of the Al adjacent to metal/oxide interface to a more stable denser nanocrystalline oxide located in the oxide layer. The resulting recrystallization ruptures in the surface and produces regions of rarefied oxide between nanocrystallites (anhydrous/amor‐ phous). It is in these regions that pore nuclei form. Earlier studies by Habazaki et al. [77] indicated the potential for the enrichment of alloying elements, dopants and/or impurities in the Al substrate adjacent to the metal/oxide interface. The enrichment layers were found to be about 1 to 5 nm thick immediately beneath the metal/oxide interface and were a consequence of the oxide growth. These enrichment layers may also be involved in the initiation of changes within the oxide layer that promote pore nucleation. In a recent investigation by Zaraska et al. [78], the presence of alloying elements in an Al alloy (AA1050) not only slowed the rate of oxide growth but also influenced structural features such as porosity, barrier layer thickness, pore diameter and pore density of the forming oxide layer.

In the early stages of the anodization process Al3+ ions migrate from the metal across the metal/ oxide interface into the forming oxide layer [83]. Meanwhile O2- ions formed from water at the oxide/electrolyte interface travel into the oxide layer. During this stage approximately 70% of the Al3+ ions and the O2- ions contribute to the formation of the barrier oxide layer [79], the remaining Al3+ ions are dissolved into the electrolyte. This condition has been shown to be the prerequisite for porous oxide growth, in which the Al-O bonds in the oxide lattice break to release Al3+ ions [80]. During the oxide formation the barrier layer constantly regenerates with further oxide growth and transforms into a semi-spherical oxide layer of constant thickness that forms the pore bottom, as shown in Figure 15 [75].

**Figure 15.** Schematic structure of anodic porous alumina (A) and a cross-sectional view of the anodized layer (B) [75].

During the formation of the porous oxide layer the anodic Al dissolution reaction is presented by:

$$\text{2Al} \rightarrow \text{2Al}^{3} + \text{6e} \text{-}\tag{9}$$

The oxidation takes place over the entire pore base and the resulting oxide material grows perpendicular to the surface, neighboring pore growth prevents growth in any other direc‐ tion. The vertical growth of the pore wall creates a columnar structure with a high aspect ratio that contains a central circular channel. This channel extends from the base of the pore to the surface of the oxide layer [81]. This upward growth of the pore wall was recently investigated by Garcia-Vergara et al. [86] in which a tungsten tracer was placed into an initial oxide layer formed by an initial anodization step. During the next stage of anodization, the position of the tracer was monitored and found to travel from the metal/oxide interface of the barrier layer located at the base of the pore towards the growing wall structure. This flowing motion of the tracer was credited to the mechanical stresses being generated by the continued formation of newoxidewithintheporebaseandtherepulsiveforcessetupbetweenneighboringporesduring the growth of the wall structure. These forces resulted from the volume expansion (by a factor of 2) during the oxidation of Al to alumina. This volumetric expansion factor results from the difference in the density of Al in alumina (3.2 g cm-2) and that of metallic Al (2.7 g cm-2). This volumetric oxide expansion at the metal/oxide interface also contributes to the hemispherical shape of the pore base. However, under normal experimental conditions, the volumetric expansion factor is less than 2. This is due to the hydration reaction that occurs at the oxide/

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electrolyte interface which results in the dissolution and thinning of the oxide layer.

The volumetric growth of the oxide layer is also dependent upon the type of electrolyte (this effect is more evident when using phosphoric or sulfuric acids), the electrolyte concentration and the electric field created by the anodizing voltage. Furthermore, a research investigation by Li et al. [85] has shown that a volume expansion factor of 1.4 could be achieved under

**Figure 16.** Schematic of ion movement during pore formation [81].

<sup>2</sup> 6H+ + 6e- 3H ® (10)

$$\text{Al} + 3\text{O}^{2-} \rightarrow \text{Al}\_2\text{O}\_3 + 6\text{e} \tag{11}$$

$$\rm{Al}^{3} + \rm{3H}\_{2}\rm{O} \rightarrow \rm{Al}\_{2}\rm{O}\_{3} + \rm{6H} + \tag{12}$$

Sum of the separate reactions at electrode: (Overall anodization of Al equation)

$$\text{2Al} + \text{3H}\_2\text{O} \rightarrow \text{Al}\_2\text{O}\_3 + \text{3H}\_2\tag{13}$$

The steady state growth results from the balance between the field-enhanced oxide dissolu‐ tion at the oxide/electrolyte interface at the base of the hemispherical shaped pores where the electric field is high enough to propel the Al3+ ions through the barrier layer and the oxide growth at the metal/oxide interface resulting from the migration of O2− and OH ions into the pore base oxide layer, as in Figure 16. This also explains the dependence of the size of the pore diameter to the electric field produced by the anodizing voltage. It should also be noted that the electric field strength in the pore walls is too small to make any significant contribution to the flow of ions. The oxidation takes place over the entire pore base and the resulting oxide material grows perpendicular to the surface, neighboring pore growth prevents growth in any other direc‐ tion. The vertical growth of the pore wall creates a columnar structure with a high aspect ratio that contains a central circular channel. This channel extends from the base of the pore to the surface of the oxide layer [81]. This upward growth of the pore wall was recently investigated by Garcia-Vergara et al. [86] in which a tungsten tracer was placed into an initial oxide layer formed by an initial anodization step. During the next stage of anodization, the position of the tracer was monitored and found to travel from the metal/oxide interface of the barrier layer located at the base of the pore towards the growing wall structure. This flowing motion of the tracer was credited to the mechanical stresses being generated by the continued formation of newoxidewithintheporebaseandtherepulsiveforcessetupbetweenneighboringporesduring the growth of the wall structure. These forces resulted from the volume expansion (by a factor of 2) during the oxidation of Al to alumina. This volumetric expansion factor results from the difference in the density of Al in alumina (3.2 g cm-2) and that of metallic Al (2.7 g cm-2). This volumetric oxide expansion at the metal/oxide interface also contributes to the hemispherical shape of the pore base. However, under normal experimental conditions, the volumetric expansion factor is less than 2. This is due to the hydration reaction that occurs at the oxide/ electrolyte interface which results in the dissolution and thinning of the oxide layer.

**Figure 16.** Schematic of ion movement during pore formation [81].

**Figure 15.** Schematic structure of anodic porous alumina (A) and a cross-sectional view of the anodized layer (B) [75].

During the formation of the porous oxide layer the anodic Al dissolution reaction is presented

2

Sum of the separate reactions at electrode: (Overall anodization of Al equation)

at the metal/oxide interface resulting from the migration of O2− and OH-

The steady state growth results from the balance between the field-enhanced oxide dissolu‐ tion at the oxide/electrolyte interface at the base of the hemispherical shaped pores where the electric field is high enough to propel the Al3+ ions through the barrier layer and the oxide growth

oxide layer, as in Figure 16. This also explains the dependence of the size of the pore diameter to the electric field produced by the anodizing voltage. It should also be noted that the electric field strength in the pore walls is too small to make any significant contribution to the flow of ions.

3

<sup>3</sup> 2Al 2Al + + 6e- ® (9)

<sup>2</sup> 6H+ + 6e- 3H ® (10)

2 3 2Al + 3O - Al O + 6e- ® (11)

2 23 2Al + + 3H O Al O + 6H+ ® (12)

2 23 2 2Al + 3H O Al O + 3H ® (13)

ions into the pore base

by:

148 Modern Surface Engineering Treatments

The volumetric growth of the oxide layer is also dependent upon the type of electrolyte (this effect is more evident when using phosphoric or sulfuric acids), the electrolyte concentration and the electric field created by the anodizing voltage. Furthermore, a research investigation by Li et al. [85] has shown that a volume expansion factor of 1.4 could be achieved under optimal anodizing parameters, independent of the electrolyte used. The porous oxide layer thickness and hence pore height can grow to many times the height of the barrier layer. It is usually during this oxide growth that electrolyte anions can integrate into the forming porous structure near the oxide/electrolyte interface, while pure alumina is predominantly found in layers close to the metal/oxide interface. It is also possible for voids to form in the pore walls during the growth of the oxide layer. Possible causes of these voids range from oxygen evolution during oxide formation to localized defects in the barrier layer. These defects produce a condensation effect that involves cations and/or metal vacancies at the metal/oxide interface, which subsequently become detached, and form the void.

**•** AAO template has been proved to be a cheap and high yield technique to produce large arrays of metals nanowires with tunable pore dimensions, good mechanical property, and

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1 Department of Metallurgy, Faculty of Engineering, Cairo University, Giza, Egypt

[1] Luther, W. Industrial Application of Nanomaterials- Chances and Risks, Future

[3] Gleiter, H. Nanostructured Materials: Basic Concepts and Microstructure. Acta Mate‐

[4] Peuloro, S, & Lincot, D. Cathodic Electrodeposition from Aqueous Solution of Dense or Open-structured Zinc Oxide Films. Advanced. Materials (1996). , 8, 166-170.

[5] Koch, C. C. Nanostructured Materials: Processing, Properties and Applications, Wil‐

[6] Bockris, J. O'M. Fundamental Aspects of Electrocrystallization, Plumn Press, New

[8] Seo, M. H, Kim, D. J, & Kim, J. S. The Effects of pH and Temperature on Ni-Fe-P Al‐ loy Electrodeposition from a Sulfamate Bath and the Material Properties of the De‐

[9] Sam, S, Fortas, G, Guittoum, A, Gabouze, N, & Djebbar, S. Electrodeposition of NiFe

[10] Abdel-karim, R, Reda, Y, Muhammed, M, Raghy, S, Shoeib, M, & Ahmed, H. Electro‐ deposition and Characterization of Nanocrystalline Ni-Fe Alloys. Journal of Nano‐

[11] Brenner, A. Electrodeposition of Alloys, chapter 1, Academic Press, New York, NY,

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2 Department of Metallurgy, Nuclear Research Center, Cairo, Anshas, Egypt

Technologies Division of VDI Technologiezentrum GmbH, (2004).

[2] Aliofkhazraei, M. Nanocoatings, chapter 1, Springer, (2011).

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good thermal stability by the electrodeposition.

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**Author details**

R. Abdel-Karim1

**References**

Diggle et al. [86].discussed the contradictory research results of the period. For example, the non- porous barrier layer was regarded as amorphous and anhydrous, while the porous layer had been found to be both amorphous and crystalline. In the case of the barrier layer, under normal anodization conditions the layer will be amorphous. However, studies by Uchi et al. [87] have shown that with the right growth conditions it was possible to have amorphous or crystalline Al oxide being produced during anodization. To form a crystalline oxide structure; an Al substrate was first immersed in boiling water to form a hydrous oxide layer [oxyhydroxide with excess water (AlOOH.H2O)]. The substrate was then anodized in a neutral borate solution at high temperatures, during which Al3+ ions move from the metal substrate to the hydrous oxide interface, where they combine and transform the hydrous oxide to crystalline Al2O3. Some of the contradictory evidence of the earlier works discussed by Diggle et al. [86] of the porous layer could be explained by the work of De Azevedo et al. [88]. In this study the structural characteristics of doped and un-doped porous Al oxide, anodized in oxalic acid was investigated using X-ray diffraction (XRD). The XRD patterns for the un-doped samples revealed several peaks associated with Al and Al2O3 crystalline phases on top of a broad peak that was approximately centered on the 2θ angle of 25°. This broad peak indicated that the synthesized layer was a highly disordered and/or amorphous Al oxide compound.
