# Preparation of Al-Mg Alloy Electrodes by Using Powder Metallurgy and Their Application for Hydrogen Production

Authors: Wen-Nong Hsu; Teng-Shih Shih; Ming-Yuan Lin
Journal: Advances in Materials Science and Engineering
 (2014)

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## Abstract

The choice of an electrode is the most critical parameter for water electrolysis. In this study, powder metallurgy is used to prepare aluminum-magnesium (Al-Mg) alloy electrodes. In addition to pure Mg and Al electrodes, five Al-Mg alloy electrodes composed of Al-Mg (10 wt%), Al-Mg (25 wt%), Al-Mg (50 wt%), and Al-Mg (75 wt%) were prepared. In water electrolysis experiments, the pure Al electrode exhibited optimal electrolytic efficiency. However, the Al-Mg (25 wt%) alloy was the most efficient when the anticorrosion effect and materials costs were considered. In this study, an ultrasonic field was applied to the electrolysis cell to improve its efficiency. The results revealed that the current increased by approximately 23.1% when placed in a 30 wt% KOH solution under the ultrasonic field. Electrochemical polarization impedance spectroscopy (EIS) was employed to evaluate the effect of the ultrasonic field on the reduction of polarization resistance. The results showed that the concentration impedance in the 30 wt% KOH electrolyte decreased markedly by 44%–51% Ω.


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## Body

## 1. Introduction

Hydrogen is a clean pollution-free and economical energy carrier, which indicates that it has the greatest potential for use as an alternative energy source. Hydrogen releases energy without producing greenhouse gases, such as CO2, and it has the highest power density among all fuels. It has high development potential, and it is a clean power source with an indefinite supply. In the 1800s, scientists generated high-purity hydrogen and oxygen by conducting water electrolysis. Water contains a large amount of hydrogen, and it is the ideal material to obtain it from. Hydrogen power is superior to other energy sources because it is renewable and can be used to generate electric power or heat. Through a chemical reaction, hydrogen can form water, which can be decomposed into hydrogen and oxygen through electrolysis. Therefore, performing water electrolysis to produce hydrogen is a crucial method for generating energy. Improving the efficiency of water electrolysis for hydrogen production is a valuable research topic.The voltage required to perform water electrolysis consists of largely reversible potential (1.23 V, 1 atm, 25°C). However, the actual decomposition potential is higher than 1.23 V. Low reaction overpotential is crucial to improving the efficiency and economic viability of water hydrolysis, because high energy consumption and a low hydrogen output are two issues affecting the applicability of water electrolysis [1]. To reduce the overpotential and increase the hydrogen output, several previous studies have discussed the effects of working parameters such as alkaline (KOH, NaOH) or acid (HCl, H2SO4) electrolytes, relative electrode distance, flow-field effect, and electrolyte temperature on the electrolytic hydrogen production efficiency. For example, Nagai et al. [2], de Souza et al. [3, 4], and Licht et al. [5] have shown that the flow field generated from electrolyte stirring resulted in a higher ion concentration on the electrode surface, thereby increasing the electrolytic efficiency. Dubey et al. [6] employed carbon nanotubes to replace graphite electrodes, to increase the efficiency of hydrogen production. Nikolic et al. [7] added cobalt and tungsten ions to an alkaline electrolyte, reduced the power consumption by 15%, and produced the same amount of hydrogen. In addition, certain studies have used additional external mechanisms to improve the efficiency of water electrolysis. For example, Lin et al. [8] applied a magnetic field to an electrolyte solution to discuss the magnetic phenomenon of electrolytes under the Lorentz force and demonstrated improvements in the polarization potential and hydrogen production efficiency. Matsushima et al. [9, 10] applied a magnetic field during electrolysis to examine the polarization overpotential curve in oversaturated electrolytes.In water electrolysis, one of the most critical factors is the choice of an electrode material. The characteristics of an ideal electrode include low operating potential, favorable electrocatalytic properties, time stability, and low cost. Platinum is widely used as an electrode material, although it is relatively expensive. Considering the cost, iron, cobalt, nickel, stainless steel, and graphite are also widely used electrode materials [11, 12]. Regarding the methods for manufacturing electrodes, powder metallurgy is a convenient and efficient technique that has numerous advantages such as low energy consumption, efficient material usage, and simple procedure. Furthermore, its products can be designed with porosity, uniform chemical composition, refractory materials, and incompatible composite materials. For this study, Al-Mg electrodes of various compositions were sintered, and their electrolytic performance was subsequently evaluated in distinct alkaline electrolytes to identify electrodes suitable for water electrolysis. Finally, we applied an ultrasonic field to accelerate the reduction of the accumulated impedance caused by the formation of numerous bubbles on the electrode surface. High-frequency longitudinal ultrasonic waves cause continuous changes in positive and negative pressure in fluid media and generate tens of thousands of microvacuum bubbles, a phenomenon known as “cavitation bubbles” [13–16]. Cavitation bubbles continuously form, extrude, and break, resulting in the disturbance and rapid degasification of the fluid. Early in the nineteenth century, metallurgists understood that applying ultrasonic energy to a molten medium would uniformly disperse impurities and have a degassing effect. This could improve the quality of cast products substantially [16, 17]. This study examined the effect of applying ultrasonic energy to various electrolyte concentrations during water electrolysis and evaluated the effect of various electrodes on the performance of hydrogen production. Electrochemical polarization impedance spectroscopy (EIS) was employed to measure the related polarization phenomena, and a camera was used to capture images of the bubble flow field.


## 2. Experimental

The electrodes used in the study were prepared using a powder metallurgy method. Pure Al and Mg powders were used as raw materials. The mean particle size of both powders was approximately 100 mesh. In addition, five alloy electrodes composed of Al-Mg (10 wt%), Al-Mg (25 wt%), Al-Mg (50 wt%), Al-Mg (75 wt%), and Al-Mg (90 wt%) were also prepared. After thoroughly mixing the various compositions of powder, the mixture was placed in a metal mold and pressed at 200 MPa for 30 s. To prevent oxidation at elevated temperatures, a quartz tube furnace was filled with protective gas (hydrogen) during the sintering process. The electrode specimens were sintered to 500°C, held at that temperature for 3 h, and then left to cool to room temperature in the furnace. The sintered electrode specimens were fabricated with a dimension of12
×
12
×
5 mm (
L
×
W
×
H
) for subsequent analysis.Because Ni electrodes are corrosion-proof as well as acid- and alkali-resistant in electrolytes, a pure Ni anode was used in this study. Seven types of electrodes were prepared as cathodes (working electrodes), with a total geometric area of approximately 144 mm2. The distance between electrodes was fixed at 30 mm. Three electrolyte concentrations (i.e., 10 wt%, 20 wt%, and 30 wt%) of KOH were used. The electrobath used in this experiment was composed of an acid- and alkali-resistant acrylic material (30
×
15
×
100 mm; L
×
W
×
H). Figure 1 shows the experimental apparatus. The AUTOLAB PGSTAT302N potentiostat of the Netherlands ECO was used for the I-V curve measurement of water electrolysis in each electrode to analyze the electrolytic performance. A 225-W ultrasonic field was introduced to the outer cell during water electrolysis. A camera was used to record the effect of the ultrasonic field on the bubble beams. In this experiment, the frequency response analyzer (FRA) module of the potentiostat was used to measure the EIS curves of the electrochemical reaction. The EIS curve was transformed into the impedance spectrum by using the Nyquist curve of the equivalent circuit. Curve fitting was performed using software to analyze the impedance distribution in the set-equivalent circuit and to obtain the impedance values. Based on these data, the following section discusses the effects of the various parameters on the impedance values during the electrochemical experimental process.Figure 1
The experiment devices. (a) Electrodes, (b) electrolysis cell, (c) outer cell, (d) potentiostat, (e) ultrasonic generator, (f) computer, (g) thermometer, and (h) camera.


## 3. Results and Discussion

### 3.1. Electrolytic Performance of the Al-Mg Electrodes

The phase diagram in Figure2 shows the microstructures of the materials used in this study. Selecting an electrode material first involves considering its electrical conductivity, because a high electrical conductivity facilitates efficient electrolysis. In this study, conductivity is expressed in accordance with the International Annealed Copper Standard (IACS). Table 1 (line A) shows the conductivity results of the electrodes. The pure Al and Mg electrodes were more conductive than the alloy composites (62 IACS and 38 IACS, resp.). However, the conductivity of the Al-Mg (50 wt%) alloy electrodes yielded substantially lower values (4 IACS), exhibiting the lowest conductivity.Table 1
The electrolytic performance of the experimental electrodes.
Property
Electrodes
Mg
Al-Mg(90 wt%)
Al-Mg(75 wt%)
Al-Mg(50 wt%)
Al-Mg(25 wt%)
Al-Mg(10 wt%)
Al
(a) Conductivity (IACS)
38
11
7
4
8
14
62
(b) Corrosion rate    (%)
0
0
0
0
0
45
99
(c) Decomposition voltage (V)
3.65
3.50
3.40
3.15
2.85
2.55
2.35Figure 2
The phase diagram of Al-Mg alloy.Electrode materials should exhibit corrosion resistance to basic electrolytes. Table1 (line B) shows the relationship between the electrolysis time and corrosion weight percentage for each electrode at a fixed voltage of 5 V in the 30 wt% KOH electrolyte for 8 h. The pure Al and Al-Mg (10 wt%) electrodes were subject to corrosion. Formula (1) shows the reaction of the pure Al sample in the KOH electrolyte. The KOH electrolyte in water was dissociated to yield K+ and OH− ions, and then the combination of Al and OH− ions resulted in Al(
OH
)
4
-, which led to corrosion. The byproduct of this chemical reaction produced hydrogen, and the product in water electrolysis was also hydrogen. If electrode consumption was not considered, the pure Al electrode produced an adequate amount of hydrogen. However, the Al-Mg (25 wt%) electrode electrolyzed in the 30 wt% KOH electrolyte for 8 h exhibited good corrosion resistance. If the corrosion resistance of the electrodes is considered, the Al content of the Al-Mg alloy electrode should be equal to or less than 75 wt%:
(1)
2
Al
(
s
)
+
2
KOH
(
s
)
+
6
H
2
O
(
aq
)
⟶
2
K
+
(
aq
)
+
2
Al
OH
4
-
(
aq
)
+
3
H
2
(
g
)


### 3.2. The I-V Curve of Al-Mg Electrodes

Figure3 shows the I-V curves of the seven electrodes in the 30 wt% KOH electrolyte. The decomposition voltages (Table 1, line C) were obtained by plotting a tangent on the I-V curve and intersecting the x-axis. The decomposition voltage of the pure Al and Mg electrodes was approximately 2.35 V and 3.65 V, respectively. In summary, an electrode with a low decomposition voltage is more efficient. As shown in Figure 3, the magnitude of the current density of the electrodes is in the order of Al > Al-Mg (10 wt%) > Al-Mg (25 wt%) > Al-Mg (50 wt%) > Al-Mg (75 wt%) > Al-Mg (90 wt%) > Mg. The pure Al electrode yielded the most favorable I-V curve, and the current density decreases with the weight percentage of Al. By contrast, the I-V curve of the pure Mg electrode indicated that it was the least efficient for electrolysis. In summary, the pure Al electrode exhibited a low decomposition voltage and optimal electrolytic efficiency, although it was susceptible to corrosion because of its high activity. Therefore, it is suitable for use as a consumable electrode. If both the corrosion property and electrolytic efficiency are considered, the preferred Al-Mg alloy electrode would be the Al-Mg (25 wt%) specimen. In other words, the increase in phase content of the intermetallic compound (Al12Mg17) in the Al-Mg electrodes facilitates corrosion resistance.Figure 3
The I-V curve of seven electrodes in 30 wt% KOH electrolyte.


### 3.3. The Effect of Ultrasound Application on the Efficiency of Water Electrolysis for the Al-Mg (25 wt%) Electrode at Different Electrolyte Concentrations

An ultrasonic wave refers to a sound pressure wave at frequencies higher than 20 kHz. Ultrasonic waves generate cyclic alternating acoustic pressures of compression and tension. When the acoustic pressure is sufficiently strong, the liquid is subjected to tensile forces during the negative cycle of the wave, and the molecules of the liquid can be pulled away from one another to form cavitation bubbles, which are transient bubbles. During the following compression cycle, the cavitation bubbles collapse violently, forming microjets and shock waves. Some of these cavitation bubbles grow rapidly under the influence of the alternating acoustic pressure and the directed diffusion of dissolved gas from the liquid, thereby forming steady bubbles. The numerous bubbles coagulate and rise to the surface of the liquid, which is called “ultrasonic degassing.”The electrolytic performance of the Al-Mg (25 wt%) electrode was examined in three electrolyte concentrations with and without ultrasound. Figures4(a)–4(c) show the I-V curves of water electrolysis at 5 V. The results revealed that the current increased by 5.3%, 18.5%, and 23.1% when the ultrasound was applied to the 10 wt%, 20 wt%, and 30 wt% KOH electrolyte concentrations, respectively. Moreover, the camera, which was used to record the bubble behaviors in the electrolytic process, revealed bubble clusters that were created through ultrasonic forced oscillation. These phenomena are easy to understand. Introducing an ultrasound to the electrolytic cell resulted in acoustic cavitation. The creation of gas bubbles (both hydrogen and oxygen) on the electrodes accelerated, and steady bubbles were formed through direct diffusion. The bubble clusters grew rapidly and detached from the electrode surface in the sound field, effectively reducing the polarization resistance in the electrolytic cell and enhancing electrolytic efficiency.The effect of applying ultrasound on the water electrolysis for Al-Mg (25 wt%) electrode. (a) 10 wt%, (b) 20 wt%, (c) 30 wt% KOH electrolyte, (d) bubbles (without ultra), and (e) bubbles (with ultra).
(a)
(b)
(c)
(d)
(e)In addition to using an I-V curve to calculate the power efficiency, a Nyquist potential impedance equivalent diagram was used to examine the relationship between the change in the polarization impedances and ultrasonic action. Figure5 shows the EIS curves measured using the constant electric displacement FRA module with an electrode spacing of 3 mm and external potential of 2.8 V. For the 10 wt% electrolyte condition without ultrasound, the EIS curve in Figure 5(a) shows two clearly defined semicircles. The results indicated that both the activation and concentration polarization increased because of the low electrical conductivity and poor hydration effect. Under a low-frequency condition, the electrochemical reaction time increased, and the activation and concentration polarization curves could be measured. Under the 20 wt% and 30 wt% electrolyte conditions, the low-frequency semicircles (Figures 5(b) and 5(c)) were not clearly defined because of the improved hydration effect. The electron and ion exchange rate between the electrodes and the electrolyte solution was high, and the overall reaction time decreased. Although the low frequencies produced longer reaction times, the polarization phenomena were minimized. In summary, applying the ultrasound to the electrolytic cell reduced polarization impedance in all cases.The Nyquist curves and polarization impedance chart at different electrolytes: (a) 10 wt%, (b) 20 wt%, (c) 30 wt%, and (d) polarization impedances.
(a)
(b)
(c)
(d)Figure5(d) shows the activation and concentration impedance at three electrolyte concentrations, which were obtained from the regression curves of the EIS curves in Figures 5(a)–5(c). Overall, the results revealed that applying ultrasonic waves to various electrolytes can effectively improve impedance. The ohm impedance, activation impedance, and concentration impedance values decreased by approximately 1%–30% Ω, 1.5%–7.6% Ω, and 44%–51% Ω, respectively. The concentration impedance values exhibited the greatest reduction because the ultrasonic field removed the hydrogen and oxygen bubbles from the electrodes, which destroyed the diffusion layer, reduced electrode fouling, and altered the absorption and surface conditions. Consequently, the ion transmission improved, the limiting current increased, and the overpotential decreased. Furthermore, an increase in ohmic impedance was obvious for the 30 wt% electrolyte concentration. Under these conditions, the hydration effect of the electrolyte improved, the electron and ion exchange rate between the electrode and electrolyte was high, and the electrochemical reaction was violent. Therefore, numerous bubbles formed between the electrodes, leading to an increase in ohmic impedance. When the ultrasound was applied to the electrolysis system, the bubbles on the electrode surface were removed rapidly, and the ohmic impedance decreased from 1.8 to 1.2 Ω.


## 3.1. Electrolytic Performance of the Al-Mg Electrodes

The phase diagram in Figure2 shows the microstructures of the materials used in this study. Selecting an electrode material first involves considering its electrical conductivity, because a high electrical conductivity facilitates efficient electrolysis. In this study, conductivity is expressed in accordance with the International Annealed Copper Standard (IACS). Table 1 (line A) shows the conductivity results of the electrodes. The pure Al and Mg electrodes were more conductive than the alloy composites (62 IACS and 38 IACS, resp.). However, the conductivity of the Al-Mg (50 wt%) alloy electrodes yielded substantially lower values (4 IACS), exhibiting the lowest conductivity.Table 1
The electrolytic performance of the experimental electrodes.
Property
Electrodes
Mg
Al-Mg(90 wt%)
Al-Mg(75 wt%)
Al-Mg(50 wt%)
Al-Mg(25 wt%)
Al-Mg(10 wt%)
Al
(a) Conductivity (IACS)
38
11
7
4
8
14
62
(b) Corrosion rate    (%)
0
0
0
0
0
45
99
(c) Decomposition voltage (V)
3.65
3.50
3.40
3.15
2.85
2.55
2.35Figure 2
The phase diagram of Al-Mg alloy.Electrode materials should exhibit corrosion resistance to basic electrolytes. Table1 (line B) shows the relationship between the electrolysis time and corrosion weight percentage for each electrode at a fixed voltage of 5 V in the 30 wt% KOH electrolyte for 8 h. The pure Al and Al-Mg (10 wt%) electrodes were subject to corrosion. Formula (1) shows the reaction of the pure Al sample in the KOH electrolyte. The KOH electrolyte in water was dissociated to yield K+ and OH− ions, and then the combination of Al and OH− ions resulted in Al(
OH
)
4
-, which led to corrosion. The byproduct of this chemical reaction produced hydrogen, and the product in water electrolysis was also hydrogen. If electrode consumption was not considered, the pure Al electrode produced an adequate amount of hydrogen. However, the Al-Mg (25 wt%) electrode electrolyzed in the 30 wt% KOH electrolyte for 8 h exhibited good corrosion resistance. If the corrosion resistance of the electrodes is considered, the Al content of the Al-Mg alloy electrode should be equal to or less than 75 wt%:
(1)
2
Al
(
s
)
+
2
KOH
(
s
)
+
6
H
2
O
(
aq
)
⟶
2
K
+
(
aq
)
+
2
Al
OH
4
-
(
aq
)
+
3
H
2
(
g
)


## 3.2. The I-V Curve of Al-Mg Electrodes

Figure3 shows the I-V curves of the seven electrodes in the 30 wt% KOH electrolyte. The decomposition voltages (Table 1, line C) were obtained by plotting a tangent on the I-V curve and intersecting the x-axis. The decomposition voltage of the pure Al and Mg electrodes was approximately 2.35 V and 3.65 V, respectively. In summary, an electrode with a low decomposition voltage is more efficient. As shown in Figure 3, the magnitude of the current density of the electrodes is in the order of Al > Al-Mg (10 wt%) > Al-Mg (25 wt%) > Al-Mg (50 wt%) > Al-Mg (75 wt%) > Al-Mg (90 wt%) > Mg. The pure Al electrode yielded the most favorable I-V curve, and the current density decreases with the weight percentage of Al. By contrast, the I-V curve of the pure Mg electrode indicated that it was the least efficient for electrolysis. In summary, the pure Al electrode exhibited a low decomposition voltage and optimal electrolytic efficiency, although it was susceptible to corrosion because of its high activity. Therefore, it is suitable for use as a consumable electrode. If both the corrosion property and electrolytic efficiency are considered, the preferred Al-Mg alloy electrode would be the Al-Mg (25 wt%) specimen. In other words, the increase in phase content of the intermetallic compound (Al12Mg17) in the Al-Mg electrodes facilitates corrosion resistance.Figure 3
The I-V curve of seven electrodes in 30 wt% KOH electrolyte.


## 3.3. The Effect of Ultrasound Application on the Efficiency of Water Electrolysis for the Al-Mg (25 wt%) Electrode at Different Electrolyte Concentrations

An ultrasonic wave refers to a sound pressure wave at frequencies higher than 20 kHz. Ultrasonic waves generate cyclic alternating acoustic pressures of compression and tension. When the acoustic pressure is sufficiently strong, the liquid is subjected to tensile forces during the negative cycle of the wave, and the molecules of the liquid can be pulled away from one another to form cavitation bubbles, which are transient bubbles. During the following compression cycle, the cavitation bubbles collapse violently, forming microjets and shock waves. Some of these cavitation bubbles grow rapidly under the influence of the alternating acoustic pressure and the directed diffusion of dissolved gas from the liquid, thereby forming steady bubbles. The numerous bubbles coagulate and rise to the surface of the liquid, which is called “ultrasonic degassing.”The electrolytic performance of the Al-Mg (25 wt%) electrode was examined in three electrolyte concentrations with and without ultrasound. Figures4(a)–4(c) show the I-V curves of water electrolysis at 5 V. The results revealed that the current increased by 5.3%, 18.5%, and 23.1% when the ultrasound was applied to the 10 wt%, 20 wt%, and 30 wt% KOH electrolyte concentrations, respectively. Moreover, the camera, which was used to record the bubble behaviors in the electrolytic process, revealed bubble clusters that were created through ultrasonic forced oscillation. These phenomena are easy to understand. Introducing an ultrasound to the electrolytic cell resulted in acoustic cavitation. The creation of gas bubbles (both hydrogen and oxygen) on the electrodes accelerated, and steady bubbles were formed through direct diffusion. The bubble clusters grew rapidly and detached from the electrode surface in the sound field, effectively reducing the polarization resistance in the electrolytic cell and enhancing electrolytic efficiency.The effect of applying ultrasound on the water electrolysis for Al-Mg (25 wt%) electrode. (a) 10 wt%, (b) 20 wt%, (c) 30 wt% KOH electrolyte, (d) bubbles (without ultra), and (e) bubbles (with ultra).
(a)
(b)
(c)
(d)
(e)In addition to using an I-V curve to calculate the power efficiency, a Nyquist potential impedance equivalent diagram was used to examine the relationship between the change in the polarization impedances and ultrasonic action. Figure5 shows the EIS curves measured using the constant electric displacement FRA module with an electrode spacing of 3 mm and external potential of 2.8 V. For the 10 wt% electrolyte condition without ultrasound, the EIS curve in Figure 5(a) shows two clearly defined semicircles. The results indicated that both the activation and concentration polarization increased because of the low electrical conductivity and poor hydration effect. Under a low-frequency condition, the electrochemical reaction time increased, and the activation and concentration polarization curves could be measured. Under the 20 wt% and 30 wt% electrolyte conditions, the low-frequency semicircles (Figures 5(b) and 5(c)) were not clearly defined because of the improved hydration effect. The electron and ion exchange rate between the electrodes and the electrolyte solution was high, and the overall reaction time decreased. Although the low frequencies produced longer reaction times, the polarization phenomena were minimized. In summary, applying the ultrasound to the electrolytic cell reduced polarization impedance in all cases.The Nyquist curves and polarization impedance chart at different electrolytes: (a) 10 wt%, (b) 20 wt%, (c) 30 wt%, and (d) polarization impedances.
(a)
(b)
(c)
(d)Figure5(d) shows the activation and concentration impedance at three electrolyte concentrations, which were obtained from the regression curves of the EIS curves in Figures 5(a)–5(c). Overall, the results revealed that applying ultrasonic waves to various electrolytes can effectively improve impedance. The ohm impedance, activation impedance, and concentration impedance values decreased by approximately 1%–30% Ω, 1.5%–7.6% Ω, and 44%–51% Ω, respectively. The concentration impedance values exhibited the greatest reduction because the ultrasonic field removed the hydrogen and oxygen bubbles from the electrodes, which destroyed the diffusion layer, reduced electrode fouling, and altered the absorption and surface conditions. Consequently, the ion transmission improved, the limiting current increased, and the overpotential decreased. Furthermore, an increase in ohmic impedance was obvious for the 30 wt% electrolyte concentration. Under these conditions, the hydration effect of the electrolyte improved, the electron and ion exchange rate between the electrode and electrolyte was high, and the electrochemical reaction was violent. Therefore, numerous bubbles formed between the electrodes, leading to an increase in ohmic impedance. When the ultrasound was applied to the electrolysis system, the bubbles on the electrode surface were removed rapidly, and the ohmic impedance decreased from 1.8 to 1.2 Ω.


## 4. Conclusion

In this study, seven electrodes were prepared using a powder metallurgy method. The current density of the obtained electrodes exhibited the following characteristic: Al > Al-Mg (10 wt%) > Al-Mg (25 wt%) > Al-Mg (50 wt%) > Al-Mg (75 wt%) > Al-Mg (90 wt%) > Mg. The experimental results revealed that the electrolytic efficiency increased with the Al content in the electrode. However, Al is easily oxidized to form Al(
OH
)
4
- in a KOH electrolyte. Based on the anticorrosion and electrolytic efficiency of the electrodes, the Al-Mg (25 wt%) electrode would be the ideal candidate; in other words, the Al content of the Al-Mg alloy electrodes should be equal to or less than 75 wt%. This electrode exhibited high corrosion resistance, and it is easy to obtain as well as economical. Furthermore, the ultrasonic wave was applied to the cells to reduce the polarization resistance. The increase in current observed for various electrolyte concentrations revealed the following tendency: 30 wt% KOH > 20 wt% KOH > 10 wt% KOH. In the 30 wt% KOH, the optimal current increased by 23.1%. The EIS curves, measured using the FRA module and the regression curves, indicated an effective improvement in polarization impedance between the electrodes under ultrasonic vibration. The concentration polarization in the 30 wt% KOH under ultrasonic conditions decreased to 44%–51% Ω during electrolysis.



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*Source: 594984-2014-11-23.xml*