Yudong Gongab,
Yang Zhaoc,
Yujin Chen*c,
Yizhi Wangad and
Chunwen Sun*a
aBeijing Institute of Nanoenergy and Nanosystems, Chinese Academy of Sciences, National Center for Nanoscience and Technology (NCNST), Beijing, 100083, P. R. China. E-mail: sunchunwen@binn.cas.cn; Fax: +86-10-82854648; Tel: +86-10-82854648
bBeijing National Laboratory for Condensed Matter Physics, Institute of Physics, Chinese Academy of Sciences, Beijing 100190, China
cCollege of Science, Harbin Engineering University, Harbin, Heilongjiang 150001, China. E-mail: chenyujin@hrbeu.edu.cn; Fax: +86-451-82519754; Tel: +86-451-82519754
dCollege of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100124, China
First published on 26th April 2016
The electroreduction of water for sustainable hydrogen production is an important process for clean energy technologies, such as water splitting and fuel cells. However, development of low-cost and efficient electrocatalysts for hydrogen evolution reaction (HER) is still a great challenge. Here we reported a kind of ultrathin chain-structured CuCo2O4 (CCO) and sulfured CuCo2O4 (S-CCO) for HER with excellent activity and good durability in alkaline solution. At a current density of 10 mA cm−2, S-CCO nanocomposite catalyst only need an overpotential of 154 mV (vs. RHE), whereas chain-structured CCO need an overpotential of 490 mV. It demonstrates that sulfured treatment is an effective approach to enhance the catalytic activity of oxide for HER.
In recently years, a variety of catalysts have been extensively studied for HER, such as alloys, carbides, sulfide, phosphides, etc.12,13 Among them, Ni-based electrodes are most popular catalyst in water electrolysis due to its good corrosion resistance in high pH value solutions compared with other transition metals, such as Fe or Co.14 However, the sluggish reaction kinetics limits their application. As reported by Zheng et al. previously,15 cobalt-based alloys or compounds show excellent performance for hydrogen adsorption. Furthermore, copper-based oxides and sulfides have not been well investigated,8 because copper is usually regarded as an inert element for HER.16
Herein, we report an ultra-thin chain-structured copper cobalt oxide/sulfide composite catalyst prepared by hydrothermal method for HER. It shows excellent activity and good durability with lower overpotentials and smaller Tafel slope in alkaline solution. These results suggest a strategy for designing non-noble metal catalysts with enhanced HER performance.
To prepare the sulfured CuCo2O4 composite catalyst, 100 mg CCO and 400 mg S powder were weighted and put into two alumina boats respectively before they were transferred to a quartz tube with a flow controller. The tube was flushed by Ar at 30–50 sccm for 30 min before it was heated to 425 °C at a heating rate of 60 °C min−1 and then maintained at 425 °C for 30 min. The furnace cooled down naturally with the stable Ar flow. The obtained product was ground lightly in an agate mortar before test.
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1. Then the slurry was coated onto a piece of carbon paper (length × diameter × thickness = 6 cm × 1 cm × 0.03 cm). The loading density of the catalyst was around 3 mg cm−2. Linear sweep voltammetry with scan rate of 5 mV s−1 was conducted in 0.1 M NaOH (deaerated by N2). For a Tafel plot, the linear portion is fit to the Tafel equation. All data have been corrected for a small ohmic drop based on impedance spectroscopy. In 0.1 M NaOH (pH 13), E(RHE) = E(SCE) + 0.21 + 0.059 × pH (V). All the potentials reported in our manuscript were calibrated to a reversible hydrogen electrode (RHE).
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Co
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O ratio is about 1
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2
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4. Therefore, it is a CuCo2O4 (CCO) phase. After sulfurization, the product consists of three phases of CuCo2O4, Cu0.33Co0.67S2 and CuCo2S4, hereafter referred to as S-CCO, as shown in Fig. 1b. It should be noted that the Cu0.33Co0.67S2 has the same crystal structure with that of CoS2 while the CuCo2O4 and CuCo2S4 have the same crystal structure with that of Co3S4. The diffraction peaks of 2 theta at 27.9°, 32.3°, 36.2°, 39.8°, 46.3°, 54.9° are indexed to the (111), (200), (210), (211), (220) and (311) planes of pyrite-typed Cu0.33Co0.67S2, respectively. The diffraction peaks of 2 theta at 26.7°, 31.5°, 38.2°, 50.3° are indexed to the (220), (311), (400) and (511) planes of linnaeite-typed CuCo2O4 and CuCo2S4 respectively. It should be noted that the sulfurization reaction should be controlled well in order to get rid of other impurities.
X-ray photoelectron spectroscopy (XPS) analysis was carried out to investigate the surface composition and valence states of Cu and Co in the as-prepared S-CCO sample. Fig. 2a shows the deconvoluted spectrum of Cu 2p, which shows two peaks at binding energy of 934 and 954 eV respectively, corresponding to Cu 2p3/2 and Cu 2p1/2.17,18 Strong satellite peaks were observed at higher binding energies is due to the spin orbit characteristics of Cu2+. This shows that the majority of Cu ions are in +2 state. The deconvoluted spectrum of Co 2p is shown in Fig. 2b. The two main peaks at binding energy of 780 and 795 eV can be assigned to Co 2p3/2 and Co 2p1/2.17–19 The XPS results indicate that the valences states of Cu and Co are still remain +2 and +3 after sulfuration, respectively.
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| Fig. 2 XPS spectra of the as-prepared S-CCO sample: (a) Cu 2p core level XPS spectrum, (b) Co 2p spectrum. | ||
The size and morphology of the product were examined by field-emission scanning electron microscopy (FESEM). Fig. 3a shows most of CCO particles are nanoneedles. The average diameter and length of the nanoneedles are about 5 nm and 100 nm, respectively. After sulfurization, parts of CCO changed morphology and became linnaeite and pyrite type to form a tri-phase catalyst with CCO covered with sulfide partly. After sulfurization, the morphology of the product did not change obviously.
Fig. 4 show the nitrogen adsorption–desorption isotherms and the corresponding BJH (Barret–Joyner–Halenda) pore size distribution curves of the obtained CCO sample. It shows a typical IV adsorption–desoprtion isotherm with H3-type hysteresis (Fig. 4a), a feature of mesoporous material. The measured Brunauer–Emmett–Teller (BET) area is about 150 m2 g−1. As shown in Fig. 4b, the average pore diameter is 47 nm, calculated from the desorption branch of the nitrogen isotherm with the BJH method. The corresponding BJH desorption cumulative volume is 0.613 cm3 g−1. The high porosity can provide more active sites for reactions.
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| Fig. 4 (a) Nitrogen adsorption–desorption isotherms and (b) the corresponding BJH pore size distribution for the CCO sample. | ||
The morphology and structure of the products were further examined by transmission electron microscopy (TEM). As shown in Fig. 5, the CCO products show chain-structured morphology, which are composed of nanoparticles with a diameter of approximately 5 nm.
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| Fig. 5 TEM images of CCO chain-structured nanocomposites: (a) overall product morphology; (b) high-magnification TEM image. | ||
Fig. 6 shows an annular dark-field (ADF) scanning transmission electron microscopy (STEM) image of the sulfured CCO sample. Fig. 6b–e are the corresponding energy dispersive X-ray spectrometry (EDX) elemental mappings of Co, Cu, O and S. It can be clearly seen that Co and Cu are distributed uniformly while S and O are not the same case. Therefore, it indicates that part of CCO particles surface was covered with sulfides.
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| Fig. 6 (a) ADF-STEM image of S-CCO, (b) and (c–f) the corresponding elemental mappings of Cu, Co, S and O taken from the area marked. | ||
Electrochemical activity of the S-CCO loaded on carbon paper was measured with a three-electrode setup in 0.1 M NaOH solution. For comparison, Pt and CCO were also examined. Fig. 7a shows the polarization curves with a sweep rate of 5 mV s−1. The Pt catalyst exhibits the expected HER activity with a near zero overpotential (η), consistent with previous report.20 The S-CCO exhibit much better catalytic activity than CCO with regard to overpotential and Tafel slope. For driving cathodic current density of 10 mA cm−2, the S-CCO only need an overpotential of 154 mV (vs. RHE), whereas CCO need an overpotential of 490 mV. Impressively, the activity of S-CCO is favorably comparable to that of most electrocatalysts in the same electrolyte.8,21,22 To further study of HER activity of the S-CCO, Tafel plots were fitted to the Tafel equation (η = a + b
log|j|), where b is the Tafel slope. As shown in Fig. 7b, the Pt catalyst exhibits a Tafel slope of 40 mV dec−1. The Tafel slope of the S-CCO is 180 mV dec−1, much lower than that of the CCO (222 mV dec−1), suggesting both electrocatalysts may follow a Volmer–Heyrovsky mechanism, in which the Volmer reaction is the rate-limiting step. It demonstrates that sulfured treatment is an effective approach to enhance the catalytic activity of oxide for HER. The long-term durability of the S-CCO was examined by electrolysis at a given potential. As shown in Fig. 7c, the cathodic current densities at an overpotential of 100 mV have no obvious degradation over 12
000 s, revealing good stability of the S-CCO catalyst. For comparison, the durability of the CCO sample is also shown in Fig. 7c. It indicates that both catalysts have excellent durability for 12
000 s test. The enhanced activity of the S-CCO samples may be resulted from the abundance of disulfide-terminated surface sites in the pyrite crystal structure.23 Jin et al. found that the disulfide anions (S22−) present in all pyrite structure are important for their high electrocatalytic activity toward the HER.23 The TEM images of the S-CCO catalyst after durability test show the morphology evolution of the catalyst, as shown in Fig. 7. It is observed that the S-CCO particles have a little bit aggregation after durability test but they are still nano-sized particles.
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