Junrong
Hou‡
ab,
Xianyun
Peng‡
*cd,
Jiaqiang
Sun
e,
Shusheng
Zhang
f,
Qian
Liu
g,
Xinzhong
Wang
*a,
Jun
Luo
b and
Xijun
Liu
*h
aInformation Technology Research Institute, Shenzhen Institute of Information Technology, Shenzhen 518172, China. E-mail: wangxz@sziit.com.cn
bInstitute for New Energy Materials & Low-Carbon Technologies and Tianjin Key Lab of Photoelectric Materials & Devices, School of Materials Science and Engineering, Tianjin University of Technology, Tianjin 300384, China
cInstitute of Zhejiang University – Quzhou, Quzhou 324000, China. E-mail: xianyunpeng@zju.edu.cn
dKey Laboratory of Biomass Chemical Engineering of Ministry of Education, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou 310027, China
eState Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, China
fCollege of Chemistry, Zhengzhou University, Zhengzhou 450000, China
gInstitute for Advanced Study, Chengdu University, Chengdu 610106, Sichuan, China
hMOE Key Laboratory of New Processing Technology for Non-Ferrous Metals and Materials, and Guangxi Key Laboratory of Processing for Non-Ferrous Metals and Featured Materials, School of Resource, Environments & Materials, Guangxi University, Nanning 530004, China. E-mail: xjliu@tjut.edu.cn
First published on 5th May 2022
Electrochemical H2 production from water splitting is an environmentally sustainable technique but remains a great challenge due to the sluggish anodic oxygen evolution reaction (OER). Replacing the OER with the thermodynamically more favorable electrocatalytic oxidation process is an effective strategy for highly efficient H2 generation. Herein, Mn-doped CoS2 has predicted an excellent bifunctional electrocatalyst for the hydrogen evolution reaction (HER) and the hydrazine oxidation reaction (HzOR). With the introduction of Mn, the Gibbs free energy of the adsorbed H* and the potential rate-limiting step (the dehydrogenation of *NH2NH2 to *NHNH2) for the HzOR process of the catalyst can be significantly reduced. As expected, the Mn-CoS2 catalyst exhibited excellent catalytic activity and robust long-term stability for the HER and HzOR. In detail, the Mn-CoS2 catalyst only acquired potentials of 46 and 77 mV versus the reversible hydrogen electrode for achieving a current density of 10 mA cm−2 for the cathodic HER and anodic HzOR, respectively. In addition, the Mn-CoS2 electrode only needs a cell voltage of 447 mV to output 200 mA cm−2 in the overall hydrazine splitting system as well as exhibits a robust long-term H2 production. This work provides theoretical guidance for the design of advanced bifunctional electrocatalysts and promotes high efficiency and energy-saving H2 production technology.
Ongoing research efforts have been devoted to developing cost-effective electrocatalysts with high activity for the HER process, many potential nanomaterials (such as transition metal phosphides,19–22 sulfides,23–26 and nitrides27,28) have been widely put forward and investigated in detail. Among these catalysts, Co-based nanomaterials, especially for the cobalt disulfide (CoS2), have been regarded as promising HER electrocatalysts due to their high conductivity and unique configuration. Despite achieving significant progress, the HER catalytic activities of Co-based catalysts are also still far less than the Pt-based catalyst. In this regard, more attention has been paid to the modulation of the electronic structure and the optimization of chemical compositions, aiming to adjust the energy band structure as well as the electronic conductivity and thermodynamic H* adsorption/desorption state. The doping strategy with transition metal ions has been proved to play a significant role in optimizing the Gibbs free energy of the adsorbed H (ΔGH*) for hydrogen adsorption of HER electrocatalysts.29–35 It has been demonstrated that the HER electrocatalytic activity of Co-based catalysts can be efficiently triggered by varied transition-metal dopants.36,37 In particular, the volcano plot based on a density functional theory (DFT) revealed that elemental Mn is the best candidate dopant to tune the adsorption behavior of H atoms on adjacent Co atoms, the dopant itself, and consequently the HER activity.38
Additionally, the anodic oxygen evolution reaction (OER) is identified as the bottleneck of water splitting. The OER suffered from a high overpotential and sluggish kinetics, which greatly limit the practical application of H2 production.39 Therefore, apart from optimizing catalysts, the electrochemical H2 production can be improved and accelerated by replacing the OER with a thermodynamically more favorable electrocatalytic oxidation process. For instance, the oxidation of hydrazine, 5-hydroxymethylfurfural (HMF),40 and urea41 have been coupled with cathodic H2O reduction to effectively reduce energy consumption toward high-purity H2 generation. Among them, hydrazine (N2H4) oxidation is the most potential candidate due to its much lower oxidation potential of −0.33 V versus reversible hydrogen electrode (vs. RHE) than that of the OER (1.23 V vs. RHE).42–44 Moreover, inert N2 is the anodic oxidation product of N2H4, which can well solve the potential security issues of O2 + H2 mixture gases in membrane-free overall water splitting. In addition, with the assistance of Earth-abundant electrocatalysts, substituted anodic hydrazine oxidation could reduce the cost and overpotential of the entire water electrolysis, resulting in high-efficiency H2 production.
Herein, taking the representative CoS2 as a model electrocatalyst for the HER, we adopted a doping strategy with an Mn atom to accelerate H2 production with the assistance of anodic N2H4 oxidation by rationally modulating the electronic structure. DFT calculations demonstrated that Mn atoms can optimize the Gibbs free energy and enhance the intrinsic activity and tremendously accelerate the kinetic process. Inspired by the theoretical analysis, we successfully prepared Mn-doped CoS2 nanotubes supported on nickel foam (Mn-CoS2). As expected, the Mn-CoS2 electrocatalyst exhibited excellent electrochemical performance with a much lower overpotential of 46 mV at a current density of 10 mA cm−1 and a small Tafel slope of 63.1 mV dec−1 for the HER in 0.1 M KOH aqueous solution. Meanwhile, as for the anodic hydrazine oxidation reaction (HzOR), Mn-CoS2 only needs a small working potential of 77 mV vs. RHE to generate a current density of 10 mA cm−1.
ΔGH* = ΔEH* + ΔEZPE − TΔS |
ΔEH* = Esurface/H* − Esurface − 1/2EH2 |
The oxidation of hydrazine to nitrogen and hydrogen occurs in the following six consecutive elementary steps:
(1)
* + N2H4 → *N2H4 |
(2)
*N2H4 → *N2H3 + H+ + e− |
(3)
*N2H3 → *N2H2 + H+ + e− |
(4)
*N2H2 → *N2H + H+ + e− |
(5)
*N2H → *N2 + H+ + e− |
(6)
*N2 → * + N2 |
After that, the as-prepared precursor was put into a ceramic boat and placed in a tube furnace. Another ceramic boat containing 0.5 g of sublimed sulfur was put on the upstream side. After vacuum treatment and filling with high-purity Ar, the furnace was heated to 300 °C for 2 h with a heating rate of 1 °C min−1 with a continuous Ar flow with a flow rate of 100 sccm. After the tube furnace was naturally cooled to ambient temperature, Mn-CoS2 was obtained. For comparison, CoS2 was also prepared by a similar approach except without the addition of MnCl2·4H2O. The areal loadings of the CoS2 and Mn-CoS2 catalyst on the nickel foam were confirmed to be 2.7 and 2.9 mg cm−2, respectively. The Mn-CoS2 catalyst with various Mn contents was optimized by adjusting the additive amount of precursor. All the chemicals were directly used after purchase without further purification.
Firstly, the HER and HzOR activity of the catalysts was investigated by linear scan voltammogram (LSV) with a scan rate of 10 mA s−1. For comparison, the commercial noble metal Pt/C catalyst was measured under the same conditions. A stability test was performed using the chronopotentiometry–time and continuous cyclic voltammetry measurement technology in 0.1 M KOH. For hydrazine-assisted water electrolysis, a symmetrical full electrolyzer was assembled by directly using Mn-CoS2 as the cathode and anode. LSV was measured at a scan rate of 10 mV s−1 in 1.0 M KOH with 0.5 M N2H4 or 1 M H2SO4 with 0.5 M N2H4. For comparison, the commercial Pt/C catalyst coated nickel foam was measured under the same conditions. All the electrocatalytic current density was normalized to the geometric area of the nickel foam (1 × 1 cm2) and all potentials were given versus reversible hydrogen electrode according to the equation: ERHE = EAg/AgCl + 0.0591pH + 0.197.
Electrochemical impedance spectra (EIS) were recorded at an open-circuit potential in a frequency ranging from 100 kHz to 10 mHz with an AC voltage amplitude of 5 mV. To determine the corresponding electrochemical surface area (ECSA), the double-layer capacitance (Cdl) of all the materials was measured in a 0.1 M KOH aqueous solution. A potential range where no apparent Faradaic process occurred was determined first using cyclic voltammetry (CV) with different scan rates of 2, 4, 6, and 8 mV s−1. The value of Cdl was then obtained from the linear curve versus scan rate.
Firstly, the electronic band structures of CoS2 and Mn-CoS2 are investigated. As shown in Fig. 1b, Mn-CoS2 maintains the metallic nature as pristine CoS2 (Fig. S2†), which would favor the electron transfer process in the electrochemical catalysis process.47 It is well known that the free energy changes of hydrogen adsorption (ΔGH*) are an effective descriptor for evaluating the HER activity of electrocatalysts. The catalysts with ΔGH* close to zero are considered promising candidates for the HER. As shown in Fig. 1c, the pristine CoS2 exhibits a ΔGH* value of −2.03 eV, indicating the strong adsorption of H* on the CoS2 surface with a bond length (Co–H) of 1.471 Å (Fig. S3†). After Mn doping, the bond length of Mn–H is extended to 1.552 Å, resulting in the ΔGH* value of Mn-CoS2 decreasing to −1.05 eV, which is much close to Pt(111), indicating its excellent thermoneutrality for the HER process.
To further analyze the change in the electron distribution of the Co–H region and Mn–H region for CoS2 and Mn-CoS2, the charge density difference (CDD) of the catalyst absorbed H* was studied as shown in Fig. 1d, where the red and blue colors represent the accumulation and depletion of electrons, respectively. As the CDD contour plots shown in Fig. 1d, much more electrons from the Mn atom are transferred to the adsorbed H* in Mn-CoS2 than that of Co in CoS2. In detail, the electrons around the H atom in Mn-CoS2 are much more than that in CoS2 due to the increased electron transfer, and the Mn site in Mn-CoS2 is a relatively electron-rich state compared with the Co site in CoS2, which is probably due to the electronic interaction between Mn and the surrounding atoms (Fig. S4†). These results indicate that the modulation of the electronic structure caused by Mn doping would synergistically promote the water adsorption strength and optimize the adsorption free energy of H*, which can facilitate the electrochemical HER process.31
Apart from the investigation of HER activity, the HzOR process over CoS2 and Mn-CoS2 surfaces was also explored using first-principles calculations. Firstly, the atomic structure adsorbed N2H4 molecule over the Co site of Mn-CoS2 and Co site of CoS2 was optimized. As shown in Fig. S5,† Mn-CoS2 displays the strongest N2H4 adsorption with a more negative binding energy of −1.65 eV than that of CoS2 (−1.48 eV). Furthermore, the charge density difference was also calculated. As the charge density difference contour plot is shown in Fig. 1e and f, it can be seen that much more electrons were transferred from the Mn site to adsorbed N2H4 and the charge redistribution was dominantly restricted around the Mn site, proving the strong adsorption of N2H4 on Mn-CoS2. This electron localization behavior of the Mn-CoS2 catalyst upon Mn doping could contribute to the enhanced catalytic activity.43,48,49
The HzOR pathway on the catalyst is further studied. As shown in Fig. 1g, it can be found that adsorption of N2H4 on the Mn site of the Mn-CoS2 surface is exothermic by −1.65 eV, lower than that of the Co site of the CoS2 surface (−1.48 eV), indicating that the electron-deficient Mn species on Mn-CoS2 would facilitate the adsorption of the N2H4 molecule.50,51 Moreover, it has been revealed that the dehydrogenation process of *NH2NH2 to *NHNH2 is the potential rate-limiting step (PLS) of the HzOR on the CoS2 and Mn-CoS2 surfaces, and the PDS barrier of Mn-CoS2 (0.459 eV) is lower than that of CoS2 (0.776 eV). Therefore, the Mn-CoS2 catalyst is preferred for propelling the electrochemical HzOR process than CoS2.
Motivated by the above promising prediction, we successfully synthesized Mn-doped CoS2 nanotube supported nickel foam (Mn-CoS2/NF). Fig. 2a illustrates the synthesis schematics of the Mn-CoS2/NF. Before the growth of Mn-CoS2, the commercial NF was cleaned with acid to remove the oxide layer. Then, the cleaned NF serves as the three-dimensional skeleton for the uniform growth of Mn-Co(OH)2 nanoarrays by a facile hydrothermal synthesis at 200 °C for 6 h. Finally, the Mn-CoS2 nanotubes were obtained by the sulfuration of Mn-Co(OH)2 with sublimed sulfur as a S source at 250 °C for 2 h (please see the Experimental section for more details). For comparison, CoS2 nanoarrays were also fabricated by a similar method except without the addition of a Mn precursor.
Scanning electron microscopy (SEM) images show that the whole surface of NF is completely covered by interconnected Mn-CoS2 nanoarrays (Fig. 2b–d). The as-prepared Mn-CoS2 sample displays a nanotube morphology with a few hundred microns in length and a diameter of about 100 nanometers, as confirmed by transmission electron microscopy (TEM) (Fig. 2e and f). A high-resolution TEM image shows the visible lattice fringes with an equal interplanar distance of 2.72 Å that corresponds to the (200) plane of cubic CoS2, revealing the high crystallization feature of the Mn-CoS2 nanotubes (Fig. 2g). Furthermore, this nanotube structure is further explored by the elemental mapping images of the energy-dispersive X-ray spectroscopy (EDS) analysis. As shown in Fig. 2h–k, the Mn signals uniformly overlap with the Co and S signals in the as-prepared Mn-CoS2 catalyst.
The crystallographic structures of the as-prepared CoS2 and Mn-CoS2 catalysts are also characterized by X-ray diffraction (XRD). As the XRD pattern is shown in Fig. 3a, the as-prepared CoS2 and Mn-CoS2 exhibit similar XRD diffraction peak positions. In detail, the diffraction peaks at 32.2°, 36.2°, 39.78°, 46.31°, 54.88°, 57.53°, 60.22°, and 62.6°, which correspond to the (200), (210), (211), (220), (311), (222), (023), and (321) planes of cubic CoS2 (JCPDS no. 89-1492). In detail, it can be observed that the XRD diffraction peaks are shifted to a high angle relative to that of CoS2 (Fig. S6†), which is caused by the incorporation of Mn atoms with a smaller atomic radius into the lattice of CoS2 by replacing partial of Co atoms, confirming the successfully doping of Mn atoms into CoS2.44 Importantly, no Mn-related phase could be detected within the XRD detection range, indicating that a Mn-source was completely inserted in the CoS2 lattice. The Mn-doping level is determined to be 2.1wt% by inductively coupled plasma mass spectrometry (ICP-MS) analysis. Furthermore, X-ray photoelectron spectroscopy (XPS) measurements are employed to investigate the chemical state of the as-prepared catalysts. As shown in Fig. 3b and c, it can be found that CoS2 and Mn-CoS2 have similar high-resolution Co 2p and S 2p spectra, revealing that Mn doping does not affect the valence states of Co and S. In detail, as for the Co 2p spectra of Mn-CoS2, the core-level peaks at binding energies of 778.7 eV, 782.3 eV, 793.6, eV and 798.6 eV correspond to Co3+ 2p3/2, Co2+ 2p3/2, Co3+ 2p1/2, and Co2+ 2p1/2, respectively.26,52 Concerning the S region of Mn-CoS2 (Fig. 3c), the signals at 162.6 and 163.9 eV are attributed to the binding energies of S 2p3/2 and S 2p1/2, respectively, which belong to the typical metal–sulfur bonds.26,52 The peak at the binding energy of 168.7 eV could represent the S–O bond arising from surface air exposure.53 Impressively, the Co2+ 3d3/2 doublet of Mn-CoS2 is shifted by ≈1.6 eV toward a higher binding energy relative to that of pristine CoS2, whereas S 2p3/2 is shifted by ≈0.3 eV toward a higher binding energy. These shifts might be attributed to that the Mn dopant can provide more electrons to S than Co after Mn doping. Moreover, the high-resolution Mn 2p XPS spectrum (Fig. 2c) displays two representative XPS characteristic peaks at 643.1 and 653.4 eV corresponding to the Mn 2p3/2 and Mn 2p1/2 with an Mn4+ oxidation state in Mn-CoS2, respectively. Based on the above XRD and XPS analysis, it can be concluded that the Mn-CoS2 catalyst was successfully synthesized.
Fig. 3 Structural characterization of the as-prepared CoS2 and Mn-CoS2: (a) XRD patterns; high-resolution XPS (b) Co 2p, (c) S 2p, and (d) Mn 2p spectra. |
To demonstrate the facilitation of catalytic reactions that arise from Mn-doping, the as-prepared Mn-CoS2 catalyst was evaluated for the HER with a three-electrode configuration in 0.1 M KOH electrolytes, where Mn-CoS2 supported on NF was directly used as the working electrode, and the reference electrode and counter electrode were the Ag/AgCl electrode (filled with saturated KCl) and the carbon rod, respectively. Firstly, electrochemical HER catalytic activity was evaluated using linear scan voltammogram (LSV) with a scan rate of 10 mA s−1. As the polarization curves are shown in Fig. 4a, the Mn-CoS2 catalyst exhibits a negligible onset potential of 7 mV vs. RHE at a current density of −1 mA cm−2 near the thermodynamic potential of the HER. Moreover, Mn-CoS2 achieved a much lower overpotential of 46 mV at a current density of −10 mA cm−2, which is much better than that of pristine CoS2 (228 mV) and comparable to those of 20 wt% commercial Pt/C catalysts (Fig. 4b), Mn-CoS2 with different Mn contents (Fig. S7†), and previously reported HER catalysts (Table S1†). Furthermore, Tafel plots were derived from the polarization curves to provide a deeper insight into the detailed mechanism of the HER of the as-prepared Mn-CoS2 catalyst. As shown in Fig. 4c, a Tafel slope of 63.1 mV dec−1 for the Mn-CoS2 catalyst is close to that of Pt/C (38.2 mV dec−1).
Furthermore, to gain insights into the interfacial charge transfer kinetics on the catalytic surface during the HER process, electrochemical impedance spectroscopy (EIS) was conducted. Fig. S8† shows the Nyquist plots of the CoS2 and Mn-CoS2 electrodes with a frequency from 100 kHz to 10 mHz. It can be found that the Nyquist plots present a typical semicircle in the high-frequency region and a straight line in the low-frequency region profiles, which can be ascribed to the charge-transfer resistance of the electrochemical H+ reaction at the electrode–electrolyte interface and the diffusion-controlled impedance, respectively.54,55 Obviously, the Mn-CoS2 electrode exhibits an enhanced electron transfer rate and faster catalytic kinetics during the HER process, eventually leading to the enhanced activity for the HER. To explore the enhanced HER activity of Mn-CoS2 relative to CoS2, electrochemical double-layer capacitances (Cdl) were measured. As shown in Fig. S9,† the cyclic voltammograms (CVs) of Mn-CoS2 and CoS2 at scan rates of 2, 4, 6, and 8 mV s−1, respectively. The Mn-CoS2 electrode achieved a Cdl value of 82.5 mF cm−2, which is 4.12 times larger than that of CoS2 (20.5 mF cm−2), implying a higher surface area and more exposed active sites for Mn-CoS2, which is beneficial for enhancing the HER activity.56,57
To assess the durability of the Mn-CoS2 catalyst, the chronopotentiometry–time measurement technology was employed. As shown in Fig. 4d, it can be seen that the Mn-CoS2 electrode can maintain a high stable overpotential at a current density of −10 mA cm−2 for 54 hours with a negligible increase (Fig. 3e). Moreover, the long-term cycling stability of Mn-CoS2 was investigated by performing continuous cyclic voltammetry (CV) at a scan rate of 100 mV s−1 in 0.1 M KOH. As shown in Fig. S10,† the HER polarization curves showed a negligible difference between the curves at the initial and after 1000 cycles, implying the superior stability of Mn-CoS2 in the long-term electrochemical process. Besides, the Mn-CoS2 catalyst after the long-term measurement was further characterized by XRD, SEM, and TEM. As shown in Fig. S11,† the crystalline structure and morphology were well preserved after the long-term electrolysis, demonstrating the robust stability of Mn-CoS2 in alkaline electrolytes.
Next, the electrochemical HzOR performances of the as-prepared catalyst were evaluated in 1.0 M KOH + 0.5 M N2H4 aqueous solutions. Meanwhile, the OER performance was also tested in a 1.0 M KOH aqueous solution. Firstly, the HzOR and OER catalytic activity was measured (Fig. 5a and Fig. S12†). As shown, the Mn-CoS2 electrode exhibits a rapid increase in the HzOR activity in the alkaline electrolyte than that of the acidic one. The comparative polarization curves of the HzOR and OER suggest a dramatic improvement of activity after the addition of N2H4, indicating a great thermodynamic advantage of the HzOR. In detail, it only needs a working potential of 77 mV vs. RHE to achieve a current density of 10 mA cm−2, which is much lower than that of the CoS2 electrode (102 mV vs. RHE). In particular, the Mn-CoS2 electrode possesses large current densities of 100 and 200 mA cm−2 and only requires the potentials of 160 and 188 mV vs. RHE, which is much larger than CoS2 (216 and 282 mV vs. RHE) and even better than the commercial Pt/C catalyst (161 and 262 mV vs. RHE), indicating that the outstanding HzOR activity of the Mn-CoS2 electrode makes it a superior HzOR electrocatalyst, which is highly comparable to previously reported HzOR electrocatalysts (Table S2†). Fast charge transfer kinetics is further demonstrated by a small Tafel slope of 47.1 mV dec−1, which is much smaller than that of CoS2 (58 mV dec−1) and much closer to that of Pt/C (41.5 mV dec−1). In addition, the current density of 10 mA cm−2 just changes slightly during a long-term test for 40 h (Fig. 5d) and the HzOR polarization curves showed a slight change between the curves at the initial and after 1000 cycles (Fig. S13†), demonstrating the high stability of the Mn-CoS2 electrode in the HzOR for practical applications.
Considering the intrinsic activities of the Mn-CoS2 catalyst, we envisioned that it could realize energy-saving H2 production by utilizing Mn-CoS2 as a bifunctional electrocatalyst toward the HER and HzOR. Fig. 6a shows the comparative LSV curves of overall hydrazine splitting (OHzS), in which significantly enhanced energy efficiency can be intuitively seen using hydrazine oxidation-assisted H2 production. Specifically, the OHzS cell using Mn-CoS2 as both the anode and cathode only demands 111, 329, and 447 mV to drive current densities of 10, 100, and 200 mA cm−2, respectively (Fig. 6b), which are much lower than the overall water-splitting theoretical value of 1230 mV. By contrast, CoS2 (405, 933, and 1227 mV) and commercial Pt/C (86, 319, and 467 mV) catalysts require a higher voltage to reach up to the current densities of 10, 100, and 200 mA cm−2 (Fig. 6b). Besides, the bifunctional Mn-CoS2 catalyst in the OHzS system can maintain higher voltage stability at various current densities (10 and 50 mA cm−2) during a continuous 24 h test (Fig. 6c). Moreover, the OHzS stability test of the Mn-CoS2 electrode was also performed for 24 h at a cell potential of 111 mV. As shown in Fig. 6, the current density retention can be determined to be 96.5%. The Mn-CoS2 electrode is highly comparable to previously reported state-of-the-art OHzS electrocatalysts (Table S3†). These results demonstrate that the Earth-abundant Mn-CoS2 catalyst as a bifunctional electrode for the HER and HzOR can efficiently save energy for H2 production by water-assisted electrolysis.
Footnotes |
† Electronic supplementary information (ESI) available: The optimized structural model, electronic band structure, DOS, charge density difference, adsorption energy, XRD pattern, EIS, CV, ECSA, LSV, and i–t curves. See DOI: https://doi.org/10.1039/d2qi00083k |
‡ These authors contributed equally to this work. |
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