Yanqiang
Li
*a,
Zehao
Yin†
a,
Ming
Cui
a,
Xuan
Liu
a,
Jiabin
Xiong
b,
Siru
Chen†
*b and
Tingli
Ma
*cd
aState Key Laboratory of Fine Chemicals, School of Petroleum and Chemical Engineering, Dalian University of Technology, Panjin Campus, Panjin 124221, China. E-mail: yanqiangli@dlut.edu.cn
bCenter for Advanced Materials Research, Zhongyuan University of Technology, Zhengzhou, 450007, China. E-mail: siruchen@zut.edu.cn
cDepartment of Materials Science and Engineering, China Jiliang University, Hangzhou, 310018, China. E-mail: tinglima123@cjlu.edu.cn
dGraduate School of Life Science and Systems Engineering, Kyushu Institute of Technology, Kitakyushu, Fukuoka 808-0196, Japan. E-mail: tinglima@life.kyutech.ac.jp
First published on 27th November 2020
Benefiting from the high electrochemical surface area brought by the 2D nanosheet structure, MoS2 has received great research attention for the hydrogen evolution reaction (HER). Recently, it has been demonstrated that by constructing a transitional metal sulfide–MoS2 heterostructure, the HER performance of the MoS2-based catalysts can be further improved. It is even possible to obtain bifunctional catalysts for both HER and oxygen evolution reaction (OER) due to the synergistic effect of the different components in the composite, the electronic effect to enable an efficient electron transfer and appropriate binding energy for the intermediates of the electrocatalytic reactions, and the surface defects on the interface of the heterostructures. Herein, we review the recent progress on the construction of the transitional metal sulfide–MoS2 heterostructure for water splitting based on non-self-supporting and self-supporting catalysts. The surface and interface parameters of the heterostructures are discussed in detail to reveal the key roles of the hybrid structures for energy conversion. We also pay special attention to the theoretical simulations based on first principles to clarify the relationships between the electrochemical performance and structure parameters. Finally, the prospects and challenges of the transition metal sulfide–MoS2 heterostructures for water splitting in the future are proposed to prompt the reasonable design of transition metal sulfide–MoS2 heterostructures for full water splitting.
Electrochemical water splitting is a very mature technology, in theory, and two half reactions are involved: oxygen evolution reaction (OER) on the anode and hydrogen evolution reaction (HER) on the cathode.8 The thermodynamic voltage for water splitting is 1.23 V at 25 °C and 1 atm.9 However, in practical applications, a much larger potential is needed to drive this reaction due to the sluggish electrochemical kinetics. Nowadays, the energy conversion efficiency of water splitting is only 56–73%, and only less than 5% hydrogen is produced by this technology.10 Therefore, it is necessary to develop efficient catalysts to accelerate the reaction rate of HER and OER. So far, Pt-based catalysts are demonstrated to be the most efficient HER catalysts,11 while Ir and Ru oxides are regarded as the most efficient OER catalysts.12 However, due to the scarcity and high price of precious metals on the earth, their large-scale commercial application is limited.13 The development of catalysts with abundant earth reserves and excellent catalytic performance has become a critical factor in the commercialization of water splitting devices.
During the exploration process, transition metal-based compounds have been greatly investigated as electrocatalysts for efficient water splitting due to their earth-abundance and decent activity.14–17 Among them, MoS2 has received a lot of attention due to its high HER performance. MoS2 shows a typical layered structure similar to graphene, with weak van der Waals interactions between adjacent S–Mo–S layers, where Mo atoms are sandwiched between sulfur atoms in a hexagonal arrangement.18 The edge position of the MoS2 layered structure has been proved by theoretical calculations to be the active site for HER. Its edge also has a large number of unsaturated S atoms, which has an adsorption free energy close to 0 for the intermediate product in the HER process, making H protons easily adsorbed and desorbed on the surface of MoS2 to generate hydrogen.19,20 When used as a HER catalyst, only a small overpotential is required for MoS2 to achieve a higher current density. However, the surface layer of MoS2 is considered to be inert, which makes the process of how to expose more edge sites a critical issue. In addition, the intrinsic conductivity of MoS2 is relatively poor, which makes the resistance of the charge transport larger, resulting in larger potentials for the reaction.21 Moreover, the poor OER performance of MoS2 makes it unable to be used as a bifunctional catalyst to catalyze the water electrolysis.
At present, constructing metal sulfide–MoS2 heterostructures through interface engineering has been demonstrated as one effective strategy to improve the catalytic performance of MoS2-based catalysts.22 Due to the different catalytic activities toward HER and OER of the different components in the composites, it is probable to obtain bifunctional electrocatalysts for both OER and HER. In addition, heterostructures usually display increased electrocatalytic activities over the single-phase counterpart due to more exposed active sites on the interface, and the synergetic effect of the different components.23 Moreover, the interaction between the various components will cause the redistribution of electrons at the heterogeneous interface, so that it has a moderate adsorption-free energy for H proton and O-containing intermediate, which is very beneficial for boosting the HER and OER performance of the composite.24–27 Due to the rapid development of metal sulfide–MoS2 heterostructures for water splitting, a review about interface engineering of the MoS2-based electrocatalysts is necessary and meaningful to summarize the recent research progress on their design and application.
In this review, we focus on the construction of transition metal sulfide–MoS2 heterostructures as bifunctional electrocatalysts for overall water splitting. After the introduction on the background of the catalytic mechanism, the preparation process and structural characteristics of the materials are outlined based on non-self-supporting and self-supporting catalysts. The enhancement effects of the heterogeneous interfaces on the HER/OER performances of the catalysts are addressed, and the possible catalysis mechanism is discussed. Finally, the prospects and challenges of transition metal sulfide–MoS2 heterostructures for water splitting in the future are proposed. It is anticipated that this review will promote the reasonable design of transition metal sulfide–MoS2 heterostructures for full water splitting and other electrochemical energy conversion systems (Tables 1 and 2).
Electrocatalyst | Electrolyte | η @ j (mV @ mA cm−2) | Tafel slope (mV dec−1) | Overall voltage (V @ mA cm−2) | Stability | Ref. | ||
---|---|---|---|---|---|---|---|---|
HER | OER | HER | OER | |||||
Co9S8@MoS2/CNFs | 0.5 M H2SO4 for HER | 190 @ 10 | 430 @ 10 | 110 | 61 | Small changes in current density after 1000 CV cycles | 47 | |
1 M KOH for OER | ||||||||
Co9S8/NC@MoS2 | 0.5 M H2SO4 for HER | 117 @ 10 | 68.8 | 12 h @ 67 mV in 1 M KOH | 51 | |||
1.0 M PBS for HER | 261 @ 10 | 126.1 | 12 h @ 117 mV in 0.5 M H2SO4 | |||||
1 M KOH for HER | 67 @ 10 | 60.3 | 12h @ 261 mV in 1.0 M PBS | |||||
MCS-HP | 0.5 M H2SO4 for HER | 175 @ 10 | 410 @ 10 in 1 M KOH | 55.6 | 90.1 | 53 | ||
1 M KOH for HER | 220 @ 10 | 115.3 | ||||||
Co9S8/MoS2@NSOC | 0.5 M H2SO4 for HER | 233 @ 10 | 96 | With the loss of 11% and 9.4% respectively after 12 h work in the acidic and alkaline media | 55 | |||
1 M KOH for HER | 194 @ 10 | 118 | ||||||
CoS2–C@MoS2-25 | 0.5 M H2SO4 for HER | 173 @ 10 | 391 @ 10 | 61 | 46 | Current density remained virtually immobile for 1000 cycles | 56 | |
1 M KOH for OER | ||||||||
CoS1.097/MoS2 | 0.5 M H2SO4 for HER | 228 @ 10 | 59 | 21 h @ 10 mA cm−2 in acidic, neutral and alkaline media for HER | 57 | |||
0.1 M PBS for HER | 341 @ 10 | 85 | ||||||
1 M KOH for HER | 249 @ 10 | 75 | ||||||
Ni9S8@MoS2 | 0.5 M H2SO4 for HER | 88 @ 10 | 49 | 20 h @ 10 mA cm−2 for HER | 64 | |||
NiS2/MoS2-RGO | 0.5 M H2SO4 for HER | 172 @ 10 | 51 | 10 h @ 10 mA cm−2 in 0.5 M H2SO4 and 1 M KOH for HER | 68 | |||
1.0 M PBS for HER | 229 @ 10 | 103 | ||||||
1 M KOH for HER | 144 @ 10 | 82 | ||||||
MoS2–NiS2/NGF | 1.0 M KOH | 172 @ 10 | 370 @ 10 | 70 | 1.64 @ 10 | 24 h @ 10 mA cm−2 | 73 | |
CuS@defect-rich MoS2 | 0.5 M H2SO4 for HER | 135 @ 10 | 50 | 10000 s @ 175 mV for HER | 76 | |||
ZnS@C@MoS2 | 1 M KOH for HER | 118 @ 10 | 55.4 | 12 h @ 30 mA cm−2 for HER | 80 | |||
MoS2 NDs/VS2 | 0.5 M H2SO4 for HER | 291 @ 10 | 58.1 | 16 h @ 300 mV for HER | 83 | |||
NiCo2S4@MoS2 | 1 M KOH for HER | 194 @ 10 | 62 | 10 h @ 10 mA cm−2 for HER | 87 | |||
MoS2/NiCoS | 1 M KOH | 189 @ 10 | 290 @ 10 | 75 | 77 | 1.50 @ 10 | 22 h @ 10 mA cm−2 | 88 |
Co,Fe–MoS2 | 1 M KOH | 113 @ 10 | 264 @ 10 | 61 | 117 | 1.49 @ 10 | 10 h @ 10 mA cm−2 | 89 |
MoS2–g-CuNi2S4 | 0.5 M H2SO4 for HER | 120 @ 10 | 29.3 | Small changes in current density after 1000 CV cycles | 90 |
Electrocatalyst | Electrolyte | Substrate | η @ j (mV @ mA cm−2) | Tafel slope (mV dec−1) | Overall voltage (V @ mA cm−2) | Stability | Ref. | ||
---|---|---|---|---|---|---|---|---|---|
HER | OER | HER | OER | ||||||
Co5Mo10Sx/CC | 1 M KOH | Carbon fiber cloth | 36 @ 10 | 153 @ 10 | 56 | 58 | 1.51 @ 10 | 12 h @ 10 mA cm−2 | 105 |
MoS2/CoS2 | 0.5 M H2SO4 for HER | Carbon fiber paper | 126 @ 10 | — | 42.6 | — | — | 10 h @ 10 mA cm−2 | 106 |
1.0 M PBS for HER | 196 @ 10 | 77.5 | |||||||
1 M KOH for HER | 97 @ 10 | 78.7 | |||||||
CoS2/MoS2 HNSAs | 1 M KOH for HER | Ni foam | 50 @ 10 | — | 76 | — | — | 70 h @ 100 mV | 110 |
CoMoSx/NF | 1 M KOH | Ni foam | 89 @ 10 | 345 @ 100 | 94 | — | 1.89 @ 500 | 25 h @ 500 mA cm−2 | 113 |
Mo-doped Ni3S2 | 1 M KOH | Ni foam | 212 @ 10 | 260 @ 10 | 98 | 85 | 1.67 @ 10 | 48000 s @ 10 mA cm−2 | 119 |
MoS2–Ni3S2 HNRs/NF | 1 M KOH | Ni foam | 98 @ 10 | 290 @ 10 | 61 | 57 | 1.50 @ 10 | 48 h @ 17 mA cm−2 | 120 |
MoS2/Ni3S2 heterostructures | 1 M KOH | Ni foam | 110 @ 10 | 218 @ 10 | 83 | 88 | 1.56 @ 10 | 10 h @ 10 mA cm−2 | 121 |
N–NiS/MoS2 | 1 M KOH | Ni foam | 71 @ 10 | — | 79 | — | — | 20 h @ 30 mA cm−2 | 125 |
p-MoS2/Ni3S2/NF | 1 M KOH | Ni foam | 99 @ 10 | 185 @ 10 | 71 | 46 | — | 35 h @ 10 mA cm−2 | 128 |
MoS2/FNS/FeNi foam | 1 M KOH | FeNi foam | 120 @ 10 | 204 @ 10 | 45.1 | 28.1 | — | 10 h @ 10 mA cm−2 for HER | 134 |
10 h @ 204 mV for OER | |||||||||
(Ni, Fe)S2@MoS2 | 1 M KOH | Carbon fiber paper | 130 @ 10 | 270 @ 10 | 101.2 | 43.2 | 1.56 @ 10 | 40 h @ 10 mA cm−2 | 135 |
CoMoNiS–NF-31 | 1 M KOH | Ni foam | 113 @ 10 | 166 @ 10 | 85 | 58 | 1.54 @ 10 | 24 h @ 20 mA cm−2 in 1 M KOH | 138 |
0.5 M H2SO4 | 103 @ 10 | 255 @ 10 | 55 | 78 | 1.45 @ 10 | Decreased from 21.7 to 17.4 mA cm−2 after 80 min in 0.5 M H2SO4 | |||
1.0 M PBS | 117 @ 10 | 405 @ 10 | 56 | 71 | 1.80 @ 10 | 20 h @ 1.80 V in 1.0 M PBS | |||
Mo(1–x)WxS2@Ni3S2 | 1 M KOH | Ni foam | 98 @ 10 | 285 @ 10 | 92 | 90 | 1.62 @ 10 | 50 h @ 10 mA cm−2 | 139 |
Volmer reaction:
H3O+ + M + e− → M–H + H2O (in acidic media) |
H2O + M + e− → M–H + OH− (in alkaline media) |
Heyrovsky reaction:
M–H + H3O+ + e− → M + H2 + H2O (in acidic media) |
M–H + H2O + e− → H2 + M + OH− (in alkaline media) |
Tafel reaction:
2M–H → 2M + H2 (Tafel reaction in both acidic and alkaline media) |
Regardless of the different reaction mechanisms, the adsorbed H is always involved in the reactions, and the free energy of H adsorption is an important parameter to evaluate the intrinsic activity of an electrocatalyst for HER. When the adsorption of H on the surface of the catalyst is too weak, the Volmer reaction is the rate-determination step. Conversely, when the adsorption of H on the surface of the catalyst is too strong, the desorption of H2 is the rate-determination step. Ideally, the free energy of H adsorption should be close to zero, like Pt.30
Compared with HER, OER (which occurs at the anode of the water electrolysis device) is a more complicated four-electron transfer process, and different intermediates (M–O, M–OH, M–OOH) are involved. The generally accepted reaction mechanisms in alkaline or acidic media are listed in the following equations. First, hydroxyl or water molecules are adsorbed on the catalyst to form M–OH. Then, M–OH continues to undergo an electron transfer to form M–O. After the formation of M–O, O2 can be produced via two routes. One is the direct generation of molecular oxygen from two M–O species, and the other involves M–O being oxidized into the M–OOH species first, then O2 is released from the M–OOH intermediate.31–34
In acidic media:
M + H2O → M−OH + H+ + e− |
M−OH → M−O + H+ + e− |
2M−O → 2M + O2 |
M−O + H2O → M−OOH + H+ + e− |
M−OOH → M + O2 + H+ + e− |
In alkaline media:
M + OH− → M−OH + e− |
M−OH + OH− → M−O + H2O + e− |
2M−O → 2M + O2 |
M−O + OH− → M−OOH + e− |
M−OOH + OH− → M + O2 + H2O + e− |
Like HER, OER involves the adsorption and desorption of oxygen-containing intermediates on the active sites.35,36 When the adsorption of O on the surface of the catalyst is too weak, the M–OH species is not easily formed. In contrast, when the adsorption of O on the active sites is too strong, M–OOH and O2 are not easy to generate. Therefore, the optimum of the adsorption free energy for the O-containing intermediates can be anticipated to enhance the OER performance of the catalysts.37–39
The other type of synthesis strategy is a two-step reaction route, where bimetallic precursors are prepared first, and the sulfurization reaction was carried out subsequently to prepare the metal sulfides. The bimetallic precursors can be metal oxides, metal hydroxides or metal organic frameworks, and the sulfurization reaction can be a hydrothermal reaction or thermal annealing in the presence of sulfur sources. For example, using ZIF-67 as the precursor, Sun and co-workers prepared carbon supported Co9S8@MoS2 hybrids by thermal annealing and sequenced solvothermal reaction.41 By in situ growth of Cu(OH)2 nanorod arrays on Co foam, and further hydrothermal reaction with sodium molybdate and thiourea, Yu and Co-workers prepared a Cu foam supported Cu2S/MoS2 heterostructure for HER.42
Second, the electronic effect is another factor that boosts the catalytic activity of heterostructure catalysts. This is because the strong electronic interaction between two different active components will efficiently reconstruct the active centers, which is favourable for yielding high catalytic activity. For example, Shao and co-workers observed electron transfer from (Ni, Fe)S2 to MoS2 in (Ni, Fe)S2@MoS2 heterostructures by X-ray photoelectron spectroscopy, and it is suggested that the electronic interaction between (Ni, Fe)S2 and MoS2 could weaken S–Hads formed on the interface, which regulates H chemisorption to facilitate the Volmer–Heyrovsky process.43 In other works, the roles of the electronic coupling effect were also observed, such as lowering the energy barrier of intermediates or achieving an appropriate binding energy for the electrocatalytic reactions.
Third, the defect effects are also observed in heterostructure catalysts. Introducing defects into the electrocatalysts is also an effective method to improve their catalytic performance. In heterostructure catalysts, the long-range orderly structures of the active species are interrupted due to the mismatch lattice arrangement; therefore, many defects can be formed. For example, Du and coworkers prepared a Co9S8/Ni3S2 heterostructure with a large number of lattice defects in the interface, and density functional theory indicates that the abundant lattice defects could boost the chemisorption of the intermediates, which greatly promoted its overall water splitting performance.44
Fig. 2 Schematic diagram of the reaction mechanism for water splitting at the cathode (HER) and anode (OER). |
Fig. 3 (a) The kinetic energy barrier profiles of HER on the MoS2 (top) and Co9S8@MoS2 (down) catalysts. The right side shows the diffusion paths of H2 on the MoS2 and Co9S8@MoS2 surfaces. (b) Optimized structures for the top view of H–MoS2. Reproduced with permission.47 Copyright 2015, Wiley-VCH. (c) Schematic illustration for the synthesis of Co9S8/NC@MoS2 polyhedrons. (d) LSV curves of NC, Co/NC, MoS2, Co9S8/NC, Co9S8/NC@MoS2, and Pt/C in 1.0 M KOH and 0.5 M H2SO4. (e) Polarization curves of the Co9S8/NC@MoS2 before and after 2000 CV cycles in 1.0 M KOH solution. Reproduced with permission.51 Copyright 2017, American Chemistry Society. (f) Schematic illustration of the fabrication of MCS-HP. (g) Mo 3d and S spectra in MoS2 and MCS-HP. (h) Co 2p in CS-HP, and MCS-HP. Reproduced with permission.53 Copyright 2018, Elsevier. |
Recently, metal–organic frameworks (MOFs), which consist of metal ion nodes and organic linkers, have attracted increased attention due to their well-defined pore structure, high surface area, and tunable porosity.48 Due to the weak coordination bonding and regular morphology of MOFs, they have been widely utilized as good precursors for the synthesis of nanostructured electrode/catalyst materials.49 As a well-known Co-based MOF, ZIF-67 has been widely investigated as a precursor for preparing Co-based catalysts.50 Li et al. synthesized hierarchical porous Co9S8/N-doped carbon@MoS2 (Co9S8/NC@MoS2) polyhedrons for HER over a broad pH range by using ZIF-67 and ammonium molybdate as precursors (Fig. 3c).51 Co9S8/NC@MoS2 retains the polyhedral structure of ZIF-67, and the layered MoS2 nanosheets are uniformly coated on the Co9S8/NC polyhedron. The Co/NC polyhedron derived by the carbonization of ZIF-67 has high porosity and active surface, which is beneficial for the nucleation and growth of MoS2 nanosheets on the Co/NC polyhedron. The coupling interface between MoS2 and the conductive carbon framework can reduce the work function of the carbon layers and optimize the electron structure, which is beneficial to accelerate the transfer of electrons. In addition, combining Co9S8 and MoS2 into a reasonably designed structure can combine the inherent properties of these two materials together, enabling Co9S8/NC@MoS2 with excellent HER activity over a broad pH range, with overpotentials of 67 at 10 mA cm−2 in 1.0 M KOH (Fig. 3d). In addition, the Co9S8/NC@MoS2 electrode exhibits an overpotential increase of only 3 mV after 2000 CV cycles to afford a current density of 10 mA cm−2, suggesting its good stability (Fig. 3e).
In addition to Co9S8/MoS2 composite materials, ZIF-67 has been used as a precursor to prepare Co3S4/MoS2 materials.52 For example, using ZIF-67 and sodium molybdate as raw materials, Lei et al. synthesized a MoS2/Co3S4 hollow polyhedral (MCS-HP) co-catalyst through the templated solvothermal method (Fig. 3f).53 The synthesized MCS-HP exhibits a well-defined polyhedral structure with molybdenum sulfide nanosheets covering the surface of Co3S4. Through XPS characterization, it can be observed that the Mo and Co peaks have shifted. The MoS2 that received electrons is in an electron-rich state, and the binding energy of Mo 3d is negatively shifted due to the shielding effect. On the contrary, due to the penetration effect, the Co 2p binding energy in the electron-deficient Co3S4 increased, demonstrating the strong interaction between MoS2 and Co3S4 (Fig. 3g and h). By appropriately modifying the d orbital electrons of the transition metal sulfides, the electrochemical catalytic activity of the catalyst can be improved. It only needs overpotentials of 175 and 220 mV to achieve a current density of 10 mA cm−2 in acid and alkali media, respectively.
In previous work, the MOF-templated synthesis of cobalt sulfide-based materials is limited due to the choice of ZIF-67 as the precursor, which requires an additional sulfurization process.54 Recently, Chen prepared the bimetallic sulfide Co9S8/MoS2 uniformly supported on N,S,O co-doped carbon (Co9S8/MoS2@NSOC) through the one-step pyrolysis of the Co-based MOF (Co-NOMOF) with thiomolybdate [Mo3S13]2− (Fig. 4a).55 The three-dimensional structure of Co-NOMOF facilitates the entry of Co nanoparticles into the carbon layer, and promotes the in situ doping of N and O atoms. Conversely, [Mo3S13]2− can introduce Mo and S sources, and further result in S doping into the carbon matrix. At the same time, it promotes the occurrence of the vulcanization process, and a Co9S8/MoS2 heterogeneous was finally achieved. The porosity of the Co9S8/MoS2@NSOC materials was investigated by N2 adsorption at 77 K, and the results show that there are mesopores and micropores in Co9S8/MoS2@NSOC. In addition, the calcination temperatures will significantly affect the pore structure of MOF-derived products. A high carbonization temperature is more beneficial to the formation of a porous structure. However, an excessively high temperature (1000 °C) will damage the porous structure, especially the mesopores to a certain extent (Fig. 4b and c). The rich pore structure can bring a large specific surface area to facilitate the transfer of electrolyte, and provide more active sites. Co9S8/MoS2@NSOC-900 exhibited remarkable catalytic performance for HER with overpotentials of 194 and 233 mV in 1 M KOH and 0.5 M H2SO4 solution at 10 mA cm−2, respectively, which is much better than the comparable catalysts, such as Co9S8, MoS2 and Co9S8/MoS2 (Fig. 4d and e). Its excellent performance can be ascribed to the unique electronic structure and lower local work function of the multi-heteroatom-doped carbon nanomaterials, the synergy between Co9S8 and MoS2, and the Co9S8/MoS2 heterogeneous interface that promotes the dissociation step of H2O.
Fig. 4 (a) Schematic illustration for the synthesis of Co9S8/MoS2@NSOC. (b) N2 adsorption–desorption isotherms of Co9S8/MoS2@NSOC. (c) Pore size distribution curves of the Co9S8/MoS2@NSOC catalysts. (d and e) LSV curves of the Co9S8/MoS2@NSOC900, Co@PC, MoS2, Co9S8, Co9S8–MoS2 materials for HER in 0.5 M H2SO4 and 1.0 M KOH solution. Reproduced with permission.55 Copyright 2018, Royal Society of Chemistry. (f) Schematic illustration of the synthesis of CoS2–C@MoS2. Reproduced with permission.56 Copyright 2019, American Chemistry Society. (g) Schematic illustration for the synthesis of CoS1.097/MoS2. Reproduced with permission.57 Copyright 2019, American Chemistry Society. |
In addition to the MOF-templated synthesis strategy, other precursors were selected to synthesize cobalt–molybdenum bimetallic sulfides with regular morphologies. Through the one-step hydrothermal and vulcanization treatment of Co–C nanofibers, Zhu et al. synthesized hierarchical CoS2–C@MoS2 core–shell nanofibers (Fig. 4f).56 The electrochemical measurements demonstrated that the conductivity and exposure of the active centers are two key factors that affect the catalytic performance of the catalyst. CoS2–C makes up for the shortcomings of MoS2 on conductivity, and has a synergistic effect with MoS2 to improve the performance of the catalyst. Sun et al. used cobalt chloride and ammonium molybdate as raw materials to synthesize porous CoS1.097/MoS2 hybrid microspheres with rich defects through a one-step vulcanization (Fig. 4g).57 Due to the synergy between CoS1.097 and MoS2, abundant defects and hierarchical interconnected microporous/mesoporous structure, the electrocatalytic activity of the CoS1.097/MoS2 hybrid microspheres show good HER performance, with overpotentials of 228, 249, and 341 mV at 10 mA cm−2 current density in 0.5 M H2SO4, 1 M KOH, and 0.1 M PBS electrolyte, respectively.
As shown above, for the synthesis of the CoSx–MoS2 heterostructure composites, direct hydrothermal reaction and MOFs templated method are usually utilized. For the direct hydrothermal reaction method, the obtained metal sulfides are usually sphere particles, which greatly restrict the exposure of active sites. Although hollow metal sulfides can be readily prepared by the MOFs templated strategy, it should be noted that the low yield and high cost of MOFs would prohibit the large-scale preparation of the composites. Therefore, a more effective synthetic strategy should be developed for the commercial application of the composites.
Using MoS2 for the in situ growth of Ni9S8, Xu et al. prepared a Ni9S8@MoS2 composite for HER.64 Due to the electronic coupling between Ni9S8 and MoS2, the charge transfer resistance for Ni9S8@MoS2 is greatly reduced. The electrochemical surface area of Ni9S8@MoS2 is also much larger than that for Ni9S8 and MoS2, demonstrating the fast electron transfer and more exposed active sites of the Ni9S8@MoS2 heterostructure (Fig. 5a–c). As a result, Ni9S8@MoS2 exhibited good HER catalytic activity, with an overpotential of 88 mV at 10 mA cm−2 and a low Tafel slope of 49 mV dec−1.
Fig. 5 (a) Schematic illustration of the heterostructure Ni9S8@MoS2 hybrid. (b) EIS Nyquist plots of Ni9S8@MoS2 and other materials. (c) Estimation of Cdl by plotting the current density variation vs. scan rate to fit a linear regression. Reproduced with permission.64 Copyright 2019, Elsevier. (d) Schematic illustration for the formation of NGF and MoS2–NiS2/NGF. (e and f) HRTEM images of MoS2–NiS2/NGF. (g) Polarization curves of MoS2–NiS2/NGF, MoS2–NiS2, NGF, Pt/C, and RuO2 in 1.0 M KOH for HER and OER. (h) Polarization curves of two-electrode overall water splitting using MoS2–NiS2/NGF/NF as both anode and cathode in 1.0 M KOH. Inset: galvanostatic measurement of the MoS2–NiS2/NGF/NF performed at a current density of 10 mA cm−2 in 1.0 M KOH. Reproduced with permission.73 Copyright 2019, Elsevier. |
The catalytic efficiency of the catalyst is affected by its conductivity. Poor conductivity will cause additional overpotentials, which will consume more energy and reduce the apparent activity of the catalyst.65–67 The combination of the MoS2/NiSx heterogeneous catalysts with high conductive carbon materials is expected to further improve the performance of the catalysts. Wang et al. synthesized a NiS2/MoS2 composite on reduced graphene oxide using NiMoO4–RGO as the precursor,68 and the tree-like NiS2/MoS2–RGO nanocomposites afford a current density of 10 mA cm−2 at small overpotentials of 172, 144 and 229 mV in acidic, alkaline and neutral solution, respectively. Xu et al. first treated graphene oxide with NH3 to obtain the N-doped reduced graphene oxide, and then loaded Ni3S4/MoS2 on the carbon support.69 The optimized sample possesses a large number of catalytic active sites for HER and high conductive 3D networks that benefit electron transfer, and excellent catalytic activity was achieved.
Integrating 2D carbon materials with metal sulfides can improve the conductivity of the materials. However, due to the van der Waals interaction and strong π–π accumulation between the graphene layers, the 2D graphene is easy to aggregate. This irreversible aggregation not only hinders the uniform dispersion of the catalyst, but also makes the surface inaccessible to the reactants and electrolytes, which is not beneficial for the improvement of the catalytic performance.70 In comparison, 3D graphene is an ideal scaffold for improving the electrocatalytic activity of the supported materials due to its high macroporosity and high conductivity.71,72 Using melamine foam for the adsorption of graphene oxide and further burning off the melamine template, Kuang et al. first prepared a 3D interconnected macroscopic porous nitrogen-doped graphene foam (NGF).73 The surface of the graphene foam with a negative charge can electrostatically adsorb Mo2+ and Ni2+ cations to form MoO2–Ni(OH)2 nanowalls on the NGF framework. Finally, after a CVD process, bimetallic sulfides of MoS2–NiS2 anchored on the 3D nitrogen-doped graphene foam (NGF) was successfully prepared and used as a bifunctional catalyst for water splitting (Fig. 5d). In comparison, the MoS2–NiS2 prepared without NGF exhibited severe agglomeration, which significantly reduced the contact area between the electrolyte and the catalyst, and hindered the release of gas products. The 3D hollow tube structure of MoS2–NiS2/NGF ensures abundant active sites and diverse paths to achieve the rapid and efficient transport of the electrolyte and gas. The TEM images clearly show that the heterointerface is formed between the (002) plane of MoS2 and (210) plane of NiS2 (Fig. 5e and f). In the electrolyte, H protons tend to be adsorbed by MoS2, while OH tends to be adsorbed by NiS2, resulting in the rapid dissociation step of H–O at the heterogeneous interface. The special catalyst delivered a current density of 10 mA cm−2 at overpotentials of 172 mV for HER and 370 mV for OER in 1.0 M KOH. Furthermore, when used in an alkaline water electrolyzer, MoS2–NiS2/NGF can produce the vigorous and continuous evolution of H2 and O2 at a current density of 10 mA cm−2 under a cell voltage of 1.64 V (Fig. 5g and h).
Although integrating carbon materials with metal sulfides could effectively improve the conductivity of the catalysts and prohibit the aggregation of MoS2, it should be noted that the real charming fascinating of MoS2 is its 2D nanosheet structure, which can expose the maximum number of active sites. Although it is possible to obtain several layers of MoS2 by exfoliation technology, the preparation of the ultrathin MSx–MoS2 nanosheet is rarely reported. It is also very significant to synthesize the few-layers and even the single layer MSx–MoS2 heterostructure catalysts to boost their catalytic performances.
Fig. 6 (a) Schematic illustration for the synthesis of CuS@MoS2. (b) Schematic illustration of the charge transfer in CuS@MoS2-DR and the proposed mechanism for HER. (c) Nyquist plots of CuS@MoS2-DR with other materials. (d) Polarization curves of CuS@MoS2-DR with other materials. Reproduced with permission.76 Copyright 2020, Elsevier. |
In addition to copper sulfide, transition metals ZnS have received extensive attention because of their excellent electrical conductivity for electrocatalysis.77–79 Liu et al. synthesized hierarchical ZnS@C@MoS2 core–shell nanostructures by the bottom-up two-step hydrothermal strategy combined selective etching method (Fig. 7a).80 As the core, ZnS is covered with a defective porous carbon shell, and ultra-thin MoS2 nanosheets are grown on the surface of the carbon shell. The coexistence of the ZnS semiconductor and the porous defect-rich carbon shell not only increases the conductivity of the material (Fig. 7b), but also separates and supports exfoliated MoS2 nanosheets, which can effectively expose a large number of catalytically active edge sites. The hierarchical ZnS@C@MoS2 core–shell nanostructures exhibited a low overpotential of 118 mV at 10 mA cm−2 for HER (Fig. 7c).
Fig. 7 (a) Schematic representation for the synthesis of ZnS@C@MoS2. (b) Nyquist plots of ZnS@C@MoS2 with other materials. (c) Polarization curves of ZnS@C@MoS2 with other materials for HER in 1.0 M KOH. Reproduced with permission.80 Copyright 2019, Elsevier. (d) Schematic illustration of the synthesis of MoS2 NDs/VS2 and pristine VS2. Reproduced with permission.83 Copyright 2018, American Chemistry Society. |
In addition, VS2 has gradually become a kind of promising electrocatalyst due to its unique electronic structure. Unlike other transition metal sulfides, VS2 shows an inherent metallic electronic ground state and unique electrical conductivity, making it a potential active HER electrocatalyst.81,82 Du et al. synthesized a layered heterostructure composed of MoS2 nanodots and metal VS2 nanosheets by in situ hydrothermal using water-soluble monolayer MoS2 nanodots as the size-controllable precursor, and sodium orthovanadate and thioacetamide as the sources of V and S, respectively.83 During the hydrothermal process, MoS2 nanodots act as a separator to inhibit the restacking of VS2 nanodots, while layered VS2 nanosheets act as a supporting skeleton to effectively hinder the agglomeration of MoS2 nanodots (Fig. 7d). MoS2 and VS2 can form a highly lattice-matched electron transfer heterojunction due to the orbital interaction. The redistribution of the charge is beneficial to stabilizing VS2, making it exhibit metallic characteristics and improve the overall conductivity. The optimized hybrid material exhibits significant electrocatalytic performance in acidic media due to its thinner flake heterostructure, higher conductivity, more catalytic active centers and higher intrinsic activity. Moreover, the LSV polarization curves before and after 1000 CV are almost the same, and the current density remains stable after 16 hours of chronoamperometry, demonstrating its good stability.
Fig. 8 (a and b) Comparison of the free energy diagram for the dominated Volmer–Heyrovsky pathways of MoS2 and MoS2/CoNi2S4 catalysts for HER in 0.5 M H2SO4 and 1 M KOH electrolytes, respectively. (c) The site-dependent PDOSs of Mo from the interface regions toward the metal Mo. (d) The site-dependent PDOSs of Ni from the interface toward metal Ni. CNS represents CoNi2S4 bulk. (e) The site-dependent PDOSs of Co from the IF regions toward the metal Co. Reproduced with permission.86 Copyright 2019, Wiley-VCH. (f) Schematic illustration of the synthesis of NiCo2S4@MoS2. (g and h) Polarization LSV curves and Tafel plots of NiCo2S4@MoS2 and NiCo2S4 in 1 M KOH. Reproduced with permission.87 Copyright 2019, Royal Society of Chemistry. (i) Schematic of the preparation of MoS2/NiCoS heterostructures. (j) Schematic illustration of the water splitting process for MoS2/NiCoS heterostructures. (k) Polarization curves for water splitting using MoS2/NiCoS and Ni foam as bifunctional catalysts in a 1.0 M KOH solution. Reproduced with permission.88 Copyright 2019, Royal Society of Chemistry. |
Using ZIF-67 as template, Song et al. synthesized hollow core–shell NiCo2S4@MoS2 polyhedrons, where MoS2 nanosheets were assembled on NiCo2S4 nanobuilding blocks (Fig. 8f).87 Compared with NiCo2S4 dodecahedrons, NiCo2S4@MoS2 exhibits better HER performance under alkaline conditions (Fig. 8g and h), indicating that the synergy between NiCo2S4 and MoS2 is beneficial to increase the catalytic activity. Together with a 3D architecture of the outer MoS2, the hollow structure prevents the adhesion of H2 bubbles to the electrode surface, thereby keeping the integrity of the necessary solid–liquid interface. Qin et al. also synthesized MoS2/NiCoS nanosheets and investigated their catalytic performance for water splitting through a MOF-templated strategy.88 The authors synthesized NiCo–MOF nanosheets first, which then reacted with (NH4)2MoS4 to generate two-dimensional porous MoS2/NiCoS (Fig. 8i). The two-dimensional porous structure of MoS2/NiCoS can expose more unsaturated S boundaries, therefore providing more active centers. At the same time, nanopores can promote the release of gas products and improve the stability of the catalyst. In addition, the multiple heterogeneous interfaces can modify the electronic structure of the catalyst, and the mixed-valence states of Ni, Mo, and Co further enhance the catalytic performance (Fig. 8j). The optimized MoS2/NiCoS catalyst exhibited overpotentials of 189 mV for HER and 290 mV for OER at 10 mA cm−2 in 1 M KOH solution. In particular, the MoS2/NiCoS catalyst only requires a voltage of 1.50 V to derive a current density of 10 mA cm−2 in a two-electrode electrolyzer (Fig. 8k).
Si et al. used Co3[Fe(CN)6]2 nano cubes as self-sacrificing templates for the in situ growth of a MoS2 nanosheet, during which process Co and Fe are successfully doped into MoS2 (Fe, Co–MoS2). The doping of Co and Fe not only create additional catalytic sites, but also could regulate the electronic structure of MoS2.89 The prepared catalyst retains the cubic geometric structure of the self-sacrificial template, and provides the comprehensive advantages of a high surface area, short charge transfer path, and easily accessible active sites. When used as bifunctional catalysts for water electrolysis, Co,Fe–MoS2 shows excellent catalytic activity with a low cell potential of 1.49 V at a current density of 10 mA cm−2. Adarakatti et al. synthesized a MoS2/CuNi2S4 composite catalyst supported on graphene for HER.90 By introducing transition metal (Cu and Ni) dopants, the adsorption affinity of the active edge to the intermediate hydrogen protons can be increased. Through detailed XPS analysis, it was proved that by anchoring the active center on the graphene framework, the exposure of the unsaturated S edge active sites can be increased, thereby significantly improving the intrinsic hydrogen evolution reaction activity of the MoS2/CuNi2S4 nanosheets.
As illustrated above, nowadays, most of the MSx–MoS2 heterostructure composites focus on Co and Ni-based sulfides, probably due to the high OER activity of cobalt sulfides and nickel sulfides. However, it should be noted that from the viewpoint of commercial application, Fe and Mn-based sulfides are more promising due to their low toxicity and low cost. Therefore, more efforts should be devoted toward developing these potential catalysts.
Compared with conventional coating catalysts, self-supporting catalysts that are in situ grown on conductive substrates can effectively avoid these defects faced by non-self-supporting catalysts.95 First, due to the strong adhesion of catalysts with the substrates, the self-supporting catalyst will not peel off even if it is cycled under high voltage for a long time. Second, the self-supporting catalysts are usually of nanowire, nanorod, nanosheet or nano bundle morphology, which can expose more active sites and facilitate gas release from its surface. Third, the conductive substrate can further speed up the charge transfer rate.96–98 Therefore, the MoS2-based self-supporting catalysts have attracted more wide research interests in recent years.99,100.
Fig. 9 (a) Schematic representation for the preparation of Co5Mo10Sx/CC. (b and c) Gibbs free energy diagrams for alkaline HER on the possible active sites of MoS2 and CoMoS catalysts. The optimized adsorption surface structures at different stages are shown in the inset. The S, Mo, Co, H, and O atoms are represented by orange, green, blue, white, and red spheres, respectively. Reproduced with permission.105 Copyright 2020, Elsevier. (d) Brief illustration of the synthetic process and structure of the MoS2/CoS2 hybrid and brief illustration of the heteroepitaxy-like growth of MoS2 on CoS2, where yellow balls, blue balls, and red balls respectively represent the S, Mo, and Co elements. (e) XPS survey spectra of MoS2/CoS2, CoS2, and MoS2. (f) Raman spectra of MoS2/CoS2, MoS2, and CoS2. (g) Schematic diagram for the band structure of CoS2 and n-type MoS2 before contact, and the ohmic contact and the charge transfer between metallic CoS2 and n-type MoS2. Reproduced with permission.106 Copyright 2019, American Chemistry Society. |
Huang et al. also studied the heterogeneous interface effects between MoS2 and CoS2. The author synthesized a 3D MoS2/CoS2 composite with a shell/core heterostructure that was in situ grown on carbon fiber paper (Fig. 9d).106 According to XPS and Raman analysis (Fig. 9e and f), compared with pure MoS2 and CoS2, the binding energy and Raman vibration peak of the MoS2 phase in MoS2/CoS2 composites shifted negatively, while the binding energy and the Raman vibration peak of the CoS2 phase shifted positively, demonstrating the electron transfer from CoS2 to MoS2. After the electron transfer in the MoS2/CoS2 heterogeneous interface, the CoS2 side forms an electrophilic region, while the MoS2 side forms a nucleophilic region. Due to the difference in electronegativity, for polar water molecules, CoS2 and MoS2 will attract negative O and positive H, respectively. This interaction will promote the cleavage of the O–H bond, thereby promoting water splitting. In addition, according to semiconductor physics, if the work function of the metal is smaller than that of the n-type semiconductor, the metal–semiconductor contact will be an ohmic contact with no obvious junction resistance, so that electrons can be smoothly transferred through the MoS2/CoS2 interface (Fig. 9g).
The optimization of the nanostructure can increase the specific surface area and expose more active sites for electrocatalysts.107–109 Shi et al. prepared a flower-like CoS2/MoS2 hetero-nanosheet array via in situ sulfurization of the CoMoO4 nanosheet array on NF (Fig. 10a).110 The usage of the CoMoO4 nanosheet array as a precursor enabled the well-maintained 3D network structure with high surface area and excellent conductivity after sulfurization (Fig. 10b). The flower-like structure can not only expose more heterogeneous interfaces, but also facilitate the contact of active sites with the electrolyte. Benefiting from the structural advantages and heterogeneous interface effects, the CoS2/MoS2 hetero-nanosheet array showed high catalytic performance for HER, with a low overpotential of 50 mV at a current density of 10 mA cm−2 in 1 M KOH (Fig. 10c).
Fig. 10 (a) Schematic illustration of the preparation of CoMoO4 and in situ sulfurization to CoS2/MoS2. (b) Nyquist plots of acid-treated Ni foam and CoS2/MoS2 in 1.0 M KOH. (c) Polarization curves of CoS2/MoS2. Reproduced with permission.110 Copyright 2020, Royal Society of Chemistry. (d) Schematic superhydrophilic/superaerophobic design of the CoMoSx/NF electrocatalysts for overall water splitting. (e) Overall water splitting polarization curves of CoMoSx/NF, MoSx/NF, IrO2–Pt/C and pristine NF electrodes at a scan rate of 5 mV s−1, respectively. (f) Catalytic stability of CoMoSx/NF for overall water splitting at 500 mA cm−2 for 100 hours. Reproduced with permission.113 Copyright 2020, Wiley-VCH. |
The water splitting reaction is a process of producing gas; if the generated bubbles cannot be released from the electrode in time, the active sites would be blocked and also impede the diffusion of the electrolyte, resulting in the poor contact between the catalyst and electrolyte.111,112 Compared with non-self-supporting catalysts, self-supporting catalysts more easily achieve surface hydrophilic/hydrophobic engineering.96 Shan et al. reported the preparation of superhydrophilic/superaerophobic amorphous CoMoSx chalcogel catalysts supported on nickel foam (NF) for overall water splitting (Fig. 10d).113 The prepared CoMoSx/NF shows superhydrophilicity, which facilitates the penetration of electrolytes, and superhydrophobicity, which promotes the fast release of the evolving gas bubbles. Moreover, the introduction of Co creates abundant active sites and defects. By employing CoMoSx/NF as bifunctional electrocatalysts, the overall water splitting device delivered 500 mA cm−2 current density at a low voltage of 1.89 V and without decay in performance for 100 hours (Fig. 10e and f).
Although self-supporting composites exhibit higher catalytic activity, it should be noted that the mass loading of the self-supporting catalysts is much higher that of the non-self-supporting catalysts, and few reports in the literature compared the mass activity of the catalysts. For future investigations, it is better to report the mass activity of the catalysts, rather than simply the area activity for self-supporting catalysts.
Fig. 11 (a) Illustration of the designed Mo-doped Ni3S2 nanosheets.119 Copyright 2018, Elsevier. (b) Illustration of the fabrication of the heterostructured MoS2–Ni3S2 HNRs/NF composites. Reproduced with permission.120 Copyright 2017, American Chemistry Society. |
The bimetallic sulfide MoS2/NiSx heterogeneous interface can adjust the intermediate species' adsorption energy. However, due to the greater electronegativity of S, the strong interaction between S and the adsorbed H hinders the Tafel/Heyrovsky step in HER. Introducing non-metallic anions to adjust the electron density and catalytic active centers of the bimetallic sulfides is a suitable strategy to improve the Tafel/Heyrovsky step of HER.122–124 Yang et al. synthesized nitrogen anion-decorated NiS/MoS2 heterostructures for HER. The interface between MoS2 and NiS can be clearly seen from the TEM image, indicating the formation of unique NiS/MoS2 hetero-interfaces. Through first-principles density functional theory calculations,125 the author first calculated the effect of N doping on the electron density of N–NiS. As shown in Fig. 12a, the density of states of N–NiS and NiS are continuous at the Fermi level, indicating the intrinsic metallic properties of N–NiS after the introduction of N atoms. Compared with NiS (−4.64 eV), the H2O dissociation free energy of N–NiS (−6.97 eV) is lower. Similarly, compared to MoS2 (0.48 eV), the H2O dissociation free energy of N–MoS2 (−0.06 eV) is also much smaller (Fig. 12b), proving that the introduction of non-metal atoms can enhance the electrocatalytic performance. By calculating the charge density difference, it is shown that the charge polarization of N–NiS and N–MoS2 causes a strong charge redistribution at the heterogeneous interface (Fig. 12c), and the ΔGH of the N–NiS/MoS2 heterojunction is close to 0, which makes it exhibit better HER catalytic performance. In addition, N–NiS/MoS2 exhibits very good stability without a noticeable decrease in the current density after 20 h chronoamperometry measurement, and the morphology of the catalysts is well maintained (Fig. 12d).
Fig. 12 (a) Calculated density of states for NiS and N–NiS. The Fermi level is set at 0 eV. (b) Adsorbed H2O dissociation configuration on the surfaces of the MoS2 (002) facet, N–MoS2 (002) facet, NiS (100) facet and N–NiS (100) facet, as well as the corresponding dissociation energies in alkaline solution. Yellow, dark blue, green, light blue, red and white balls represent the S, Ni, Mo, N, O and H atoms, respectively. (c) The charge density difference in the heterostructures of N–NiS/MoS2. The purple and blue isosurfaces represent the charge accumulation and depletion in the space, respectively. (d) Current density versus time (i–t) curves of N–NiS/MoS2 recorded for 20 h at 30 mA cm−2. Inset: polarization curves before and after the i–t test.125 Copyright 2019, Royal Society of Chemistry. (e–i) Contact angle of the as-prepared catalysts. The calculated hydrogen adsorption free energy changes for NiS, N–NiS, MoS2, and N–MoS2. Reproduced with permission. (e–i) Contact angle of the as-prepared catalysts: (e) NF, (f) MoS2/NF, (g) Ni3S2/NF, (h) MoS2/Ni3S2/NF, and (i) p-MoS2/Ni3S2/NF. (j and k) Picture of (j) MoS2/Ni3S2/NF and (k) p-MoS2/Ni3S2/NF during the reaction under the same electrocatalytic condition. Reproduced with permission.128 Copyright 2018, American Chemistry Society. |
The H2O adsorption on the surface of the catalysts is the first step in the water splitting process, and this step is affected by the wettability of the material surface. Hydrophilic catalysts can adsorb water molecules well. The better the hydrophilicity, the better the compatibility with water; an improved wettability can strongly enhance the water splitting performance.126,127 Li et al. synthesized a superhydrophilic porous MoS2/Ni3S2 catalyst grown on nickel foam (p-MoS2/Ni3S2/NF) through electrodeposition and the solvothermal reaction.128 The author proved the hydrophilicity of the materials and the relationship between hydrophilicity and pore structure through the contact angle test. As shown in Fig. 12e–i, Ni3S2/NF, MoS2/NF and NF all exhibit hydrophobicity, whose contact angle is greater than 90°. Conversely, the contact angle of nonporous MoS2/Ni3S2/NF is 70°, and a water droplet can be quickly absorbed by MoS2/Ni3S2/NF within 0.5 s. As for p-MoS2/Ni3S2/NF, water droplets are completely adsorbed as soon as they touch the surface of the catalyst, demonstrating its superhydrophilicity. During the reaction, a large number of O2 and H2 bubbles gathered in the non-porous MoS2/Ni3S2/NF. In contrast, no large bubbles were observed on the p-MoS2/Ni3S2/NF catalyst. This was probably due to the quick adsorption of water that promoted the squeeze of gas bubbles (Fig. 12j and k).
Using FeNi foam as a substrate for the growth of MoS2, Wu et al. synthesized MoS2/Fe5Ni4S8 heterostructures and investigated their performance for water splitting. The Fe5Ni4S8 (FNS) is in situ grown at the interface during the synthesis of MoS2.134 XPS measurements showed that the Mo 3d5/2 and 3d3/2 feature peaks shifted negatively, indicating the strong electronic interactions between FNS and MoS2. The synthesized MoS2/FNS/FeNi foam achieved a current density of 10 mA cm−2 at very low overpotentials of 120 and 204 mV for HER and OER, respectively (Fig. 13a and b). In addition to the high catalytic activity, the MoS2/FNS/FeNi also possesses higher HER stability than that of Pt/C (72.6% vs. 63.2% current retention) and comparable OER stability with IrO2 (Fig. 13c and d). The author clarified the influence of the MoS2/FNS heterogeneous interface on the enhancement for HER and OER through density functional theory calculations. First of all, for HER, the author found that compared to the H adsorption energy (−0.649 eV) on the (103) plane of MoS2, the H adsorption energy on the (103) plane at the S edge sites of FeNi–MoS2 is −1.575 eV, which leads to the tendency of the H protons to be adsorbed on the S boundary sites of the MoS2/FNS heterogeneous interface, thereby enhancing the HER performance. Secondly, for OER, the OH chemisorption energy of the uncoordinated Fe sites on Mo–Fe9S8 is −2.921 eV, which is lower than that of Fe9S8 (−0.940 eV). Similarly, for Mo–Ni9S8, the OH chemisorption energy at the uncoordinated Ni site is −2.438 eV, which is lower than that of Ni9S8 (−1.839 eV). These results prove that the MoS2/FNS heterogeneous interface facilitates the absorption of H atoms and OH groups, consequently enhancing the performances for HER and OER. As shown in Fig. 13e, the author gives the mechanisms of HER and OER on MoS2/FNS.
Fig. 13 (a and b) Polarization curves of the MoS2/FNS/FeNi foam, FNS/FeNi foam, FeNi foam, and MoS2/FTO in 1 M KOH for HER and OER, respectively. (c) Chemisorption models and corresponding adsorption energy of H and OH on the surfaces of MoS2, Fe9S8, Ni9S8, MoS2/FNS (Fe, Ni–MoS2 model), MoS2/Fe9S8 (Mo–Fe9S8 model), and MoS2/Ni9S8 (Mo–Ni9S8 model) heterostructures. (d) Current density versus time (i–t) curves of the MoS2/FNS/FeNi foam and MoS2/FNS/FeNi foil for HER and OER. (e) Illustration for the fabrication of (Ni, Fe)S2@MoS2 heterostructures. Reproduced with permission.134 Copyright 2018, Wiley-VCH. (f) Illustration for the fabrication of (Ni, Fe)S2@MoS2 heterostructures. (g) In situ Raman spectra of (Ni, Fe)S2@MoS2 at different potentials at range of 2000–2700 cm−1, (h) In situ Raman spectra at 2000–2700 cm−1 for (Ni, Fe)S2@MoS2, (Ni, Fe)S2 and MoS2. (i) LSV curves of two-electrode cell assembled by different materials (inset: the optical image of two-electrode setup). (j) Stability test of different electrolytes for (Ni, Fe)S2@MoS2. Reproduced with permission.135 Copyright 2019, Elsevier. |
Liu et al. synthesized (Ni, Fe)S2@MoS2 heterostructures for HER and OER through a two-step method. First, NiFe–LDH nanosheets supported on carbon fiber paper were synthesized by hydrothermal method. Then, thioacetamide and sodium molybdate were added to generate (Ni, Fe)S2 nano-boxes covered with layers of MoS2 nanosheets (Fig. 13f).135 The author recorded the formation process of S–Hads through in situ Raman spectra and revealed that the heterogeneous interface formed between trimetallic sulfides is favored by the adsorption of H and the formation of S–Hads, therefore boosting its overall water splitting performance (Fig. 13g and h). Using (Ni, Fe)S2@MoS2 to assemble a water splitting device, the electrolyzer only needs 1.56 V to achieve a current density of 10 mA cm−2 (Fig. 13i). In addition, by adjusting the interface between (Ni, Fe)S2@MoS2 and the electrolyte through introducing S ions into the electrolyte, the leaching of atomic S in the sulfides can be effectively relieved, and the stability of the catalysts can be significantly improved (Fig. 13j).
NiCo-based composites also showed excellent OER activity.136,137 Yang et al. synthesized a hierarchical co-assembly of interacting MoS2 and Co9S8 nanosheets attached on Ni3S2 nanorod arrays, which are supported on nickel foam by hydrothermal method using nickel foam as the substrate and Ni source, thiourea as the S source, and cobalt sulfate and sodium molybdate as the Co and Mo sources, respectively (Fig. 14a).138 When the ratio of Mo:Co is 1:3, the obtained CoMoNiS–NF-31 shows that Co9S8 and MoS2 nanosheets are directly grown on Ni3S2 nanorods, and there is no excess nanosheet to form an aggregation. This structure can make full use of the active centers. In addition, Co9S8, MoS2 and Ni3S2 completely cover the original NF surface, which improves the durability of the 3D frame structure, making CoMoNiS–NF-31 display an outstanding balance between the catalytic activity and stability, according to the activity-stability factor. The author investigated the influence of the MoS2/Co9S8 heterogeneous interface on the OER catalytic activity through density functional theory calculations (Fig. 14b–d). The two structures of the MoS2 layer parallel and perpendicular to the Co-terminated Co9S8 interface were chosen to study the charge transfer in OER. The results show that when Co9S8 is combined with MoS2, the Fermi level will decrease, and electrons will be transferred from Co9S8 to MoS2 through sulfur atoms at the Co-terminated interface (Fig. 14e). By calculating the O*, OH* and OOH* intermediates at different surface positions, the author estimates that the Gibbs free energy of the four electrochemical reaction steps occurred in OER on the Co9S8 surface in the Co9S8/MoS2 (Fig. 14f). It was found that when Co9S8 transfers electrons to MoS2, the binding energy of the OER adsorption species changes and the overpotentials decrease, indicating that the OER activity of Co9S8 strongly depends on the existence of heterogeneous interfaces with other transition metal sulfides. The CoMoNiS–NF-31 demonstrates the best electrocatalytic activity, giving ultralow overpotentials (113, 103, and 117 mV for HER and 166, 228, and 405 mV for OER) to achieve a current density of 10 mA cm−2 in alkaline, acidic, and neutral electrolytes, respectively.
Fig. 14 (a) Schematic illustration of the synthesis and growth of hierarchical CoMoNiS–NF-xy composites via one-pot hydrothermal method. (b and c) DFT-optimized structures of the MoS2/Co9S8 interfaces: (b) MoS2 (001) parallel to Co9S8 (001) and (c) MoS2 (001) perpendicular to Co9S8 (001). Atom colors: Mo, black; Co, blue; and S, yellow. Co-termination at the interface results in the most stable structure. (d) Top view of the Co9S8 (001) surface sites used for DFT calculations of the adsorbed O*, OH*, and OOH* species. (e) Calculated densities of the electronic states for the MoS2/Co9S8 interfaces with Co termination and with Co9S8. (f) Gibbs free energy changes for the four steps of OER at 0 V vs. standard hydrogen electrode. Reproduced with permission.138 Copyright 2019, Royal Society of Chemistry. |
Mo and W have similar electronic structures. According to theoretical studies, the introduction of foreign metal atoms with similar atomic radius and electronic configuration will inevitably lead to the imbalance of the local Coulomb force, and the derivative disturbance from the rearrangement of atoms will generate additional exposed edge sites. Therefore, the introduction of W will cause changes in the electronic structure of Mo-based materials and improve the overall conductivity and catalytic activity. Zheng et al. synthesized few-layered Mo(1−x)WxS2 hollow nanospheres-modified Ni3S2 heterostructures through the one-step hydrothermal reaction.139 The layered hollow structure of Mo(1−x)WxS2 not only exposes a large number of accessible active sites, but also is conducive to the mass and charge transfer during the reaction. The doping of W establishes a ternary sulfide coupling interface, which enables a strong electronic interaction between Mo(1−x)WxS2 and Ni3S2 to optimize the electronic structure at the interface and improve the conductivity of the ternary sulfide. As a result, the Mo(1−x)WxS2@Ni3S2 heterostructure exhibited good bifunctional performance, with a cell voltage of 1.62 V to deliver a current density of 10 mA cm−2 for water splitting.
As a branch in the development of water splitting catalysts, MoS2 based multi-metal sulfides have received a lot of attention in recent years and outstanding performances were achieved. However, we could not ignore some of the shortcomings and challenges in the current research, and some of the more critical points should be addressed in future investigations.
(i) Insufficient understanding of the reaction mechanism. Although great progress has been made in developing MoS2-transitional metal sulfides for water-slitting, the catalytic mechanism is still not clear. Nowadays, the most frequently proposed mechanism is the electron transfer between the different metal sulfides that promotes the H or OH adsorption. However, it should be noted that the desorption step of the products is still very important and the related investigated is rare. In addition, the interaction between the heterogeneous interfaces composed of multiple metals needs to be studied systematically to clearly explain how the so-called “synergistic effect” occurs. Moreover, the metal sulfides are an unstable species, especially under electrochemical oxidization conditions, like the metal phosphides and metal selenides. It is proposed that the metal sulfides will transform into metal (hydro)oxides during the reaction process. However, this is ignored in most of the current literature. Therefore, it is urgent to clarify the real active sites and catalytic mechanism. The use of theoretical calculations and in situ technology, coupled with the proof of experimental results, will help research studies in better understanding the mystery of water splitting.
(ii) Systematic research is still lacking. Although many of the metal sulfides have been composited with MoS2 to investigate the performance of the catalysts, a systematic approach is still lacking nowadays. It is well known that there are many crystalline phases for metal sulfides. For example, CoS, CoS2, Co3S4 and Co9S8 are common cobalt sulfides and each of them have been composited with MoS2, and many catalytic data have been collected. However, it should be noted that the electrocatalysts are in various nanostructures, morphologies, crystallinity, and combination mode with MoS2. Therefore, we could not compare the performance of the catalysts effectively. One of the major difficulties is that the synthesis of various crystalline-phased metal sulfide–MoS2 composites with the same nanostructures, morphologies, crystallinity is very challenging. In addition, optimizing the ratio of the metal sulfides and MoS2 in the heterostructure to achieve the best performance is rare, and lots of work should be done to reveal this. Theoretical calculations may be a good strategy to selectively predict the best catalysts for saving time and labor costs.
(iii) More effective and cost-effective supports should be developed. For self-supporting catalysts, nowadays, the most widely utilized supports are Ni foam and carbon cloth. For the use of Ni foam supports, it is inevitable to introduce NiSx in the catalysts, which not only limit the diversity of the composites, but also bring difficulties in understanding the catalytic mechanism due to the complicated compositions and interfaces of the catalysts. The utilization of carbon as supports could avoid the above issues. However, the high cost of carbon cloth hinders its widespread applications. Therefore, it is still urgent to develop more diverse and cost-effective supports, especially the supports that involve easy-to-implement hydrophilic/hydrophobic engineering to achieve improved catalytic performance based on the advantaged of the substrates.
(iv) The evaluation criteria need to be improved. At present, most of the evaluations for water splitting catalysts are based on the overpotential under 10 mV cmgeo−2. Although this standard can roughly distinguish the performance of the catalyst, the area of the working electrode is not equivalent to the area used by the catalyst. Moreover, this evaluation standard is based on different loadings and various test conditions. It is also difficult to compare the performance of the catalysts based on different literature studies. Therefore, standard testing conditions should be established for better comparison of the performance of catalysts, and at least the authors should clearly describe the test conditions in their manuscripts. Furthermore, nowadays most of the literature studies are focused on evaluating the performance of the catalysts in aqueous condition in the single cell, where the mass transportation is limited and the oxygen and hydrogen is mixed. For practical application, a membrane-based electrolyzer would be more efficient and the related investigation is very rare. Therefore, it is more significant to construct a membrane-based electrolyzer to evaluate the activity and practical application of the catalysts in the future.
(v) The nanostructures of the catalysts need to be optimized. The structure of the catalyst has a great influence on its electrocatalytic performance. On the one hand, a larger specific surface area means more active sites. On the other hand, an excellent structure can optimize the mass transfer capacity during the catalytic process, leading to better kinetic performances. The water splitting is a process of producing gas, which makes the requirement for the mass transfer capacity of the catalyst higher. However, at the current stage, it is still challenging to effectively construct porous structures, especially hierarchical structures that possess both high specific surface area and fast mass transport. Therefore, more effective strategies should be developed to construct superior nanostructure catalysts for water splitting.
Footnote |
† These authors contributed equally to this work. |
This journal is © The Royal Society of Chemistry 2021 |