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Journal of Advanced Marine Engineering and Technology - Vol. 48 , No. 2

[ Original Paper ]
Journal of Advanced Marine Engineering and Technology - Vol. 47, No. 5, pp. 226-230
Abbreviation: JAMET
ISSN: 2234-7925 (Print) 2765-4796 (Online)
Print publication date 31 Oct 2023
Received 26 Aug 2023 Revised 06 Sep 2023 Accepted 18 Sep 2023
DOI: https://doi.org/10.5916/jamet.2023.47.5.226

Effect of metal ratios on oxygen evolution reaction activity in binary hydroxide electrocatalysts
Seo Hyun Park1 ; Yoo Sei Park
1Undergraduate Student, Department of Advanced Material Engineering, Chungbuk National University (seohyeon.p01@gmail.com)

Correspondence to : Assistant Professor, Department of Advanced Material Engineering, Chungbuk National University, Chungdae-ro 1, Seowon-Gu, Cheongju, Chungbuk 28644, Republic of Korea, E-mail: yspark@chungbuk.ac.kr, Tel: +82-43-261-2418


Copyright © The Korean Society of Marine Engineering
This is an Open Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/by-nc/3.0), which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Funding Information ▼

Abstract

Electrochemical water splitting is a promising technology to produce hydrogen energy from water utilizing electricity. However, the sluggish kinetics of an oxygen evolution reaction (OER) hinder the achievement of high energy efficiency, acting as a barrier to the widespread adoption of electrolysis technology. Herein, we have developed CuxCoy(OH)2 by incorporating Cu into Co(OH)2. Furthermore, we systematically analyzed the structural and electrochemical characteristics based on the ratio of Cu to Co. Despite incorporating Cu into Co(OH)2, the nanosheet shape was relatively well-preserved. Nevertheless, an excessive Cu content in CuxCoy(OH)2 led to the transformation of nanosheets into polygonal shapes. Increasing Cu content improved OER activity, but excessive Cu diminished OER activity, resulting in changes in surface shape and crystal structure. This study highlights the significance of compositional optimization in developing binary hydroxide-based OER electrocatalysts.


Keywords: Hydrogen, Oxygen evolution reaction, Water splitting, Electrocatalysis, Water electrolysis

1. Introduction

Water electrolysis is a sustainable and eco-friendly technology that enables large-scale green hydrogen production without carbon emission. This process involves two half-reactions: an oxygen evolution reaction (OER, 4OH→ O2 + 2H2O + 4e) and a hydrogen evolution (HER, 2H2O + 2e→ 2OH + H2). While the HER directly contributes to hydrogen production, the OER primarily determines the overall efficiency of water electrolysis. The intrinsic sluggish kinetics of OER causes a large overpotential for water electrolysis, resulting in low energy efficiency. Therefore, a highly active electrocatalyst for OER is required to achieve high-efficiency water electrolysis.

Precious metal-based electrocatalysts such as RuO2 and IrO2 are considered the best OER electrocatalysts owing to their high catalytic activity for OER. However, their usage is limited because of their high cost and scarcity. To address these challenges, a wide variety of non-precious metal-based electrocatalysts have been developed, such as transition metal oxide [6][8][17], transition metal phosphide [12][21], transition metal sulfide [14], and transition metal hydroxide [2][4][9][22]. Among them, transition metal hydroxides have demonstrated significant promise as low-cost and active OER electrocatalysts because they can be synthesized at low temperatures while delivering high performance. Among various hydroxides, Ni(OH)2 and Co(OH)2 have been identified to possess good OER activity [4][13]. However, their OER activity is relatively poor compared to precious metal-based electrocatalysts. A modification of the electronic structure is necessary to enhance the catalytic activity for OER, which can be achieved by introducing a second metal element. Cu, in particular, is known for its excellent electron conductivity and exists in two oxidation states, +1 and +2, making it a suitable element to modify the electronic structure of Ni(OH)2 or Co(OH)2.

So far, transition metal hydroxides have been synthesized through various methods, such as hydrothermal methods [3], coprecipitation [5], corrosion engineering [11][20], and electrodeposition [15][16]. Among these methods, electrodeposition offers distinct benefits compared to other processes. This process can be performed at room temperature, is simple, and requires a short time for synthesizing the transition metal hydroxide. Moreover, by controlling the potential, time, and composition of dissolved metal salts in the electrodeposition solution, a different nanostructure can be obtained [7][19].

Here, we systematically investigated the effect of the ratio of Cu and Co in CuxCoy(OH)2 for OER. Co(OH)2 without Cu exhibited a nanosheet shape, and CuxCoy(OH)2 with an appropriate amount of Cu introduced well-maintained nanosheet shape. Furthermore, as the amount of Cu increased, it enhanced OER activity. However, excessive Cu introduction completely altered the surface shape, accompanied by a decline in the OER activity. This study highlights the significance of compositional optimization in developing binary hydroxide-based OER electrocatalysts.


2. Experiment
2.1 Preparation of CuxCoy(OH)2

CuxCoy(OH)2 was prepared on nickel foam (NF) through electrodeposition. To systematically analyze the effect of the composition of Cu and Co in CuxCoy(OH)2, the ratio of Cu2+ ion and Co2+ ion in the solution for electrodeposition was controlled (Cu2+:Co2+ = 0:2, 0.2:0.8, 0.4:0.6, and 0.8/0.2). Before electrodeposition, NF was etched in 5 M HCl for 15 min to remove the surface oxide layer and then rinsed with deionized water (DI water). The metal ion concentration in the solution for electrodeposition was 50 mmol, where Cu(NO3)2⋅6H2O, Co(NO3)2⋅6H2O, and DI water (50 mL) were mixed under magnetic stirring for 30 min at 25 ℃. NF was adopted as a working electrode, and a titanium-felt was utilized as a counter electrode. A reference electrode was a saturated calomel electrode (SCE). The electrodeposition was carried out at 25 ℃ for 5 min by applying a constant potential of -1 V. Subsequently, the electrodeposited NF was rinsed with DI water and then dried in an oven.

2.2 Materials Characterization

The surface morphologies of CuxCoy(OH)2 were observed by field emission scanning electron microscopy (FE-SEM, CZ/MIRAI LMH, TESCAN). The crystal structure of CuxCoy(OH)2 was characterized by Cu Kα radiation in the range of 10–80° (2θ) utilizing X-ray diffraction (XRD, UltimalV, Rigaku).

2.3 Electrochemical Characterization

All electrochemical measurements were performed in a three-electrode system under a 1.0-M KOH solution. The CuxCoy(OH)2 was employed as the working electrode, and a graphite rod was utilized as a counter electrode. A Hg/HgO (1 M KOH) electrode was adopted as the reference electrode. Linear sweep voltammetry was performed at a scan rate of 1 mV s-1 to obtain polarization curves, and 100% iR was corrected. The measured potential was calculated utilizing the Nernst equation: ERHE = EHg/HgO + 0.0591 × pH + 0.098. Electrochemical impedance spectroscopy was performed at a potential of 1.88 V (vs. RHE) from 10 kHz to 1 Hz. Durability was tested at a current density of 100 mA cm-1 for 180 h.


3. Results and Discussion

The surface morphologies of CuxCoy(OH)2 are presented in Figure 1. Cu0Co1(OH)2 exhibited a nanosheet shape, and similar nanosheet shapes were observed for Cu0.2Co0.8(OH)2 and Cu0.4Co0.6(OH)2. However, noticeable differences were observed owing to the varying Cu content. As the Cu ratio increased, the nanosheets became thicker and transformed into polygonal shapes. Interestingly, the surface of Cu0.8Co0.2(OH)2 differed significantly from the others, taking the form of particles rather than nanosheets [18]. EDS mapping images of Cu0Co1(OH)2, Cu0.2Co0.8(OH)2, Cu0.4Co0.6(OH)2, and Cu0.8Co0.2(OH)2 are presented in Figure 2ad. These images enabled us to analyze the element distribution, and the results confirmed the uniform distribution of Cu, Co, and O in all four samples. Furthermore, EDS analysis revealed a clear correlation between the increasing concentration of dissolved Cu2+ ion in the electrodeposition solution and a corresponding rise in the Cu content within CuxCoy(OH)2 (Table 1).


Figure 1: 
SEM images of (a) Cu0Co1(OH)2, (b) Cu0.2Co0.8(OH)2, (c) Cu0.4Co0.6(OH)2, and (d) Cu0.8Co0.2(OH)2


Figure 2: 
EDS mapping images of (a) Cu0Co1(OH)2, (b) Cu0.2Co0.8(OH)2, (c) Cu0.4Co0.6(OH)2, and (d) Cu0.8Co0.2(OH)2

Table 1: 
Composition of CuxCoy(OH)2 by EDS analysis
Sample Cu (at %) Co (at %)
Cu0Co1(OH)2 0 100
Cu0.2Co0.8(OH)2 73 27
Cu0.4Co0.6(OH)2 82 18
Cu0.8Co0.2(OH)2 85 15

Remarkably, in all samples, the atomic percentage (at %) of Cu was higher than that of Co. This phenomenon can be attributed to the faster nucleation of Cu-based hydroxides compared to Co-based hydroxides during the initial stages of the electrodeposition process. As the electrodeposition process initiates, copper-based hydroxides form first, followed by the growth of CuxCoy(OH)2 on top of them. Consequently, the composition of all samples from the bulk catalyst layer exhibits a relatively higher quantity of Cu.

To investigate the crystal structure of CuxCoy(OH)2, X-ray diffraction (XRD) patterns were obtained and presented in Figure 3. The distinctive peaks at 44.5°, 51.8°, and 76.4° correspond to characteristic peaks of metallic nickel (JCPDS: 00-004-0850). Moreover, the cobalt hydroxide phase (Co(OH)2, JCPDS: 00-046-0605) was observed in Cu0Co1(OH)2, Cu0.2Co0.8(OH)2, Cu0.4Co0.6(OH)2, and Cu0.8Co0.2(OH)2. Notably, in the XRD pattern of Cu0.8Co0.2(OH)2, additional peaks were observed besides Co(OH)2, which were indexed to copper(I) oxide (JCPDS: 98-003-1057) and metallic copper (JCPDS: 98-005-3247). Cu2O was electrochemically precipitated owing to an excess of copper ions in the electrodeposition solution, and metallic Cu was deposited while continuously exposed to a reduction current [18].


Figure 3: 
XRD patterns of Cu0Co5(OH)2, Cu1Co4(OH)2, Cu2Co3(OH)2, and Cu4Co1(OH)2

The electrocatalytic activity of CuxCoy(OH)2 for OER was evaluated in a three-electrode system utilizing a 1.0-M KOH electrolyte, as illustrated in Figure 4(a). The overpotential (η) required to achieve a current density of 10 mA/cm2 was compared to assess the catalytic activity. The overpotential of Cu0Co1(OH)2 was measured at 324 mV. The OER activity was improved as the amount of copper in CuxCoy(OH)2 increased. The overpotential of Cu0.2Co0.8(OH)2 and Cu0.4Co0.6(OH)2 was 299 mV and 293 mV, respectively, which were 25 mV and 31 mV lower than that of Cu0Co1(OH)2. However, an excessive Cu content in Cu0Co1(OH)2 led to an unexpected rise in the overpotential. This observation can be attributed to the significant presence of Cu2O rather than the active Co-based hydroxide species. As Cu2O exhibits poor OER activity compared to Co-based hydroxides, its presence contributed to the increased overpotential [10][23].


Figure 4: 
(a) Polarization curves of Co(OH)2 and CuxCo5-x(OH)2 for OER. (b) Tafel plots of Co(OH)2 and CuxCo5-x(OH)2. (c) Comparison of overpotential at 10 mA cm-2 and Tafel slopes of Co(OH)2 and CuxCo5-x(OH)2. (d) Durability test of Cu0.4Co0.6(OH)2 at 100 mA cm-2 for 180 h

To gain deeper insights into the OER, we investigated the Tafel slopes derived from the polarization curves, as illustrated in Figure 4(b). The Tafel slope represents the rate-determining step (RDS) in the OER, with smaller values indicating faster reaction kinetics. The Tafel slope of Cu0Co1(OH)2 was calculated to be 70 mV dec-1. Interestingly, the introduction of Cu reduced the value of the Tafel slope. Cu0.2Co0.8(OH)2 and Cu0.4Co0.6(OH)2 exhibited Tafel slopes of 63 mV dec-1 and 55 mV dec-1, respectively, indicating that the introduction of Cu into Co(OH)2 enhance the OER kinetics [1]. However, Cu0.8Co0.2(OH)2 demonstrated a Tafel slope of 85 mV dec-1, which is 15 mV dec-1 higher than that of Cu0Co1(OH)2, indicating that the introduction of excess copper rather reduces the OER kinetics. The overpotentials and Tafel slopes for the samples were summarized in Figure 4(c). Durability of Cu0.4Co0.6(OH)2 test was performed at 100 mA/cm2 for 180 h, as illustrated in Figure 4(d). There was no significant change for 180 h, indicating good durability for OER.


4. Conclusion

This study investigated the changes in surface morphology and catalytic activity for OER based on the ratio of Cu and Co in CuxCoy(OH)2. Even with the introduction of Cu into Co(OH)2, the nanosheet shape was relatively well-preserved. However, an excessive Cu content in CuxCoy(OH)2 led to the transformation of nanosheets into polygonal shapes. XRD analysis confirmed that an excess of Cu2+ ions in the electrodeposition solution leads to the precipitation of Cu2O. CuxCoy(OH)2 (x:y = 0.4:0.6) exhibited enhanced OER activity compared to Cu0Co5(OH)2. However, Cu0.8Co0.2(OH)2, where Cu2O is present, demonstrated poor OER activity. This study demonstrates the significance of compositional optimization in developing binary hydroxide-based OER electrocatalysts.


Acknowledgments

This research was supported by Chungbuk National University Korea National University Development Project (2022).

Author Contributions

Seo Hyun Park conducted the experiments, analyzed the data, and led the manuscript writing. Yoo Sei Park developed the intellectual concept, and provided supervisory guidance on experiments, data interpretation, and manuscript refinement.


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