1. Introduction
Due to the contamination and global warming problems, it is necessary to search for alternative environmentally friendly energy sources and decrease the concentration of CO
2 in the atmosphere
[1][2][3]. The utilization of nonprecious metal electrocatalysts for water splitting and CO
2 fixation for producing high-value-added fuels or chemicals may be the ultimate solution for sustainable and clean hydrogen energy, tackling the challenges posed by rising CO
2 levels, and realizing a closed carbon cycle
[4]. Proper electrocatalysts are extremely useful for improving the reaction rate of CO
2 conversion to its reduced oxidation states, CO and formate/formic acid. From the perspective of reactivity, CO
2 is chemically inert, and the initial bond energy of C=O is 806 kJ mol
–1, so the conversion of CO
2 into various products is a difficult problem in thermodynamics. Therefore, to make CO
2 conversion happen at a reasonable rate, the potential energy necessarily needs to be much greater than the thermodynamic values. Once the reaction is started, CO
2 can be converted into a mixture of products, mainly including carbon monoxide (CO), methane (CH
4), ethylene (CH
2CH
2), methanol (CH
3OH), ethanol (C
2H
5OH) formic acid (HCOOH), and acetate (CH
3COOH). In addition, hydrogen is a by-product produced at a potential close to the potential for CO
2 reduction
[5][6][7][8][9]. However, the electrocatalysts for the CO
2 reduction reaction (CO
2RR) and water splitting face some problems, such as low product selectivity, poor faradaic efficiency (FE), and/or hard experimental conditions (in acidic media)
[10][11]. In particular, the catalytic activity and selectivity of non-precious metal catalysts are generally much lower than those of noble metal catalysts
[12]. The activity of catalysts is not only related to the composition and structure but also to the dimension or size. The most direct effect of the decrease in dimension or size is the change in the number of active sites. Compared to conventional nanoparticles, single-atom catalysts (SACs) have the advantages of unique electronic structure, strong metal-support interactions (SMSIs), and plenty of accessible active sites and thus can significantly improve catalytic activity and selectivity
[13][14][15]. Therefore, SACs have shown prominent activity in various electrochemistry processes, including CO
2RR
[16][17], oxygen evolution reaction (OER)
[18][19], and hydrogen evolution reaction (HER)
[20][21]. However, since the surface energy increases with the decrease in particle size, the single atoms tend to aggregate into clusters or nanoparticles
[22][23], which leads to degraded functions. Hence, it is indispensable to anchor the isolated atoms onto the appropriate supports to build stable configurations with atomic distribution
[24][25]. On one hand, proper supports can serve as stabilizing functions via metal-support interactions
[26]. The strong metal–support interactions can effectively tune the electronic structure of SACs to improve the electrocatalytic activity and selectivity
[27][28][29]. Two-dimensional materials are recognized as ideal supports for SACs and as preferable alternatives for catalysts due to their unique electronic properties, high specific surface area, and substantial number of active sites
[30][31][32][33]. For example, Mn supported on 2D VTe
2 exhibits excellent catalytic performance for both HER and OER
[34]. Recent advances have demonstrated that 2D materials can improve the performance of SACs and the inhomogeneity of active sites
[35][36][37].
Two-dimensional molybdenum disulfide (MoS
2), as the representative of transition metal dichalcogenides (TMDCs), has attracted much attention for HER, OER, and CO
2RR due to its unique structure and easy functionalization
[38][39]. In addition, owing to the high earth abundance, low price, and high HER catalytic activity, 2D MoS
2 is regarded as a promising alternative for noble metals for water splitting
[40]. In addition to water splitting, 2D MoS
2 has a great potential application in CO
2RR because Mo-exposed edges can enhance the chemisorption of the reactants and thus improve the electrochemical catalysis with a low overpotential of CO
2RR (about ~54 mV) and high selectivity (the reduction product is only CO)
[39][41]. However, the electrocatalytic performance of pristine 2D MoS
2 is still not satisfactory mainly due to the lack of active sites at its basal plane and low conductivity. For example, MoS
2 edges show poor oxygen evolution reaction (OER) activity
[42], and the pristine basal plane of MoS
2 is inert to the electrochemical reduction of CO
2 [43]. Therefore, the successful combination of 2D MoS
2 and single-atom metal can not only minimize the drawbacks and maximize the advantages of the individual components; more importantly, in addition to the desired performances, some novel functions may be generated for enhancing electrocatalytic CO
2RR and overall water splitting.
Recently, single-atom metal/2D MoS2 hybrid nanomaterials have been booming in heterogeneous electrocatalysis, due to well-defined located metal centers, unique metal–support interaction, and identical coordination environment. However, there have been only a few studies on the systematic summarization of the nanomaterials for electrocatalytic CO2RR and overall water splitting.
2. Synthesis Methods of Single-Atom Metal/2D MoS2 Hybrid Nanomaterials
The catalytic performances are determined by concrete improvements of synthetic methodologies
[44]. The most widely employed approaches for SACs are pyrolysis, atomic layer deposition (ALD) method, physical vapor deposition (PVD), wet-chemistry strategy, and electronic deposition
[45][46][47]. However, it is still hard to manipulate atoms in a highly accurate way for the control synthesis of theoretically designed SACs due to ultrahigh surface free energy. The synthesis methodologies for 2D MoS
2 can be divided into two categories: top-down and bottom-up methods. The former mainly includes chemical vapor deposition (CVD) and solvothermal or hydrothermal methods
[48][49][50][51][52]; the latter includes mechanical exfoliation, chemical or electrochemical exfoliation methods, and liquid-phase exfoliation
[53]. However, the number of successful cases for single-atom metal/2D MoS
2 hybrid nanomaterials is still limited compared to the synthesis methods for single-atom metal modified 3D supports, SACs preparation, and/or 2D materials. The methods for single-atom metal/2D MoS
2 hybrid nanomaterials are derived from the approaches for SAC@3D supports, such as pyrolysis and coprecipitation. Considering that the common synthetic methods of SACs or 2D materials have been discussed in depth in previous reviews, this re
vise
warch focuses on some novel methods for single-atom metal/2D MoS
2 hybrid nanomaterials, including the one-pot chemical method, the electrochemical process, and the polyoxometalate template-based synthetic strategy (
Figure 1).
Figure 1. Several common synthesis methods of single-atom metal/2D MoS2 hybrid nanomaterials.
2.1. One-Pot Chemical Method
The principle of this method is directly to mix the precursors of SACs and 2D MoS
2 for the following reactions under inert gas (e.g., Ar). The typical processes are described as follows: firstly, all precursors (e.g., (NH
4)
6Mo
7O
24·
4H
2O, H
2PtCl
6, and CS
2) are dissolved in a certain amount of deionized water to form a homogeneous solution
[20]; then, the resulting solution is transferred to a Teflon-lined stainless autoclave under Ar and maintained at a high temperature for a certain reaction time.
The one-pot method has the advantages of simple operation and saving synthetic costs. In addition, the catalysts prepared by this method can have sulfur vacancies and the doping features of metal atoms at the same time
[54]. Until now, Cu@1T-MoS
2, Ni@1T-MoS
2, Fe@1T-MoS
2, and Co@1T-MoS
2 have been easily prepared through this method
[55].
2.2. Electrochemical Process
The electrochemical process is used to synthesize SAC-modified 2D MoS
2 via electrochemical etching of big-size metal precursor. Taking the single-atom cobalt (Co) array modified 2D MoS
2 as an example, firstly 2D MoS
2 and Co nanodisks (NDs) are synthesized using standard solvothermal procedures and standard air-free procedures, respectively. Then, the combination of Co NDs and 2D MoS
2 is realized via an assembly process. Finally, single-atom Co array covalently bound onto distorted 1T-MoS
2 nanosheets (denoted as SA Co-D 1T-MoS
2) via Co-S bonds can be synthesized through electrochemical cyclic voltammetry (CV) leaching of Co nanodisks (NDs). In addition to electrochemical CV leaching, the electrochemical deposition can be used to synthesize the nanocomposites of SACs modified 2D MoS
2, such as Pt, Cu, Sn, and Pd anchored on the 2D MoS
2, because these single metal atoms (from metal ions in the electrolyte solution) can be introduced onto the MoS
2 monolayer driven by applying the bias potential
[56].
2.3. Polyoxometalate Template-Based Synthetic Strategy
Highly purified and stable metallic 1T-MoS
2 can be obtained via a hydrothermal method which introduces organic sulfur sources into (NH
4)
6Mo
7O
24·4H
2O (denoted as Mo
7). Here, Mo
7 is a precursor that is a butterfly-shaped metal oxide cluster, and it belongs to the
β-isomer of Anderson-type polyoxometalates (POMs). In addition, its unique structure makes it possible to tune the chemical environment of 1T-MoS
2 with various metal atoms. Using Anderson-type polyoxometalates ([XH
6Mo
6O
24]
n−) as precursors, atomically designing metal doping sites onto metallic 1T-MoS
2 can be achieved. [XH
6Mo
6O
24]
n− is denoted as XMo
6 (X = Fe
III, Co
III,
n = 3; X = Ni
II,
n = 4)
[53].
3. Applications of Single-Atom Metal/2D MoS2 Hybrid Nanomaterials
3.1. Electrochemical CO2 Reduction
Electrocatalytic CO
2RR includes three steps, namely, the chemisorption of CO
2 on the surface of electrocatalysts, the transfer of high-energy electrons and protons between two elements to break C=O bonds, and the desorption of products from the surface of the electrocatalysts
[57]. For the hybrid system composed of single-atom metals and 2D MoS
2, CO
2RR more frequently occurred on metal, and the reaction paths or products are strongly dependent on the components of metal. These reaction products or paths include three types: (1) the reduction of CO
2 to CO (e.g., on Au or Ag), (2) the reduction of CO
2 to formic acid (e.g., on Sn and Pb), and (3) the reduction of CO or carbon–oxygen compounds to hydrocarbons or alcohols (e.g., on Cu, Fe, and Mn) (
Table 1).
Table 1. Summary of various single-atom metals supported at 2D MoS2 for electrochemical CO2 reduction.
Catalyst
|
Potential Determining Steps
|
Limiting Potentials (V)
|
Overpotential (V)
|
Production for Catalysts
|
Ref.
|
Fe@MoS2
|
*HCOO → *HCOOH
|
−0.39
|
0.56
|
CH4
|
[58]
|
Co@MoS2
|
*HCOO → *HCOOH
|
−0.24
|
0.41
|
CH4
|
[58]
|
Ni@MoS2
|
CO2 → *HCOO
|
−0.45
|
0.62
|
CH4
|
[58]
|
Cu@MoS2
|
*OCH3 → CH4 + *O
|
−1.05
|
1.22
|
CH4
|
[58]
|
Ru@MoS2
|
*CO → *CHO
|
−0.73
|
0.9
|
CH4
|
[59]
|
Pd@MoS2
|
CO2 → *HCOO
|
−0.96
|
1.13
|
CH4
|
[60]
|
Pt@MoS2
|
CO2 → *HCOO
|
−0.50
|
0.67
|
CH4
|
[60]
|
3.2. Electrochemical Water Splitting
In a conventional water electrolyzer, HER reaction occurs at the cathode and H
2 is separated out, while OER reaction occurs at the anode and O
2 is separated out (
Figure 2a)
[61][62][63]. Under standard conditions, a thermodynamic potential of 1.23 V is required to drive electrochemical water splitting (
Figure 2b) for HER and OER. However, in real conditions, the input potential of water splitting in practical electrolyzers is much larger than 1.23 V. In general, a high-performance electrocatalyst for water splitting is still focused on noble-metal-based catalysts (e.g., Pt for HER and IrO
2 or RuO
2 for OER) (
Table 2); however, it is necessary to develop noble metal-free electrocatalysts or decrease the loading amount of noble metals electrocatalysts because of the prohibitive cost and scarce reserve. For the reaction mechanisms (e.g., the Volmer–Heyrovsky mechanism) or paths for HER used in calculation models, there are three elementary steps regarding interactions between the water dissociates and a reactive hydrogen intermediate (absorbed hydrogen on the catalyst surface, H
ad), including the Volmer step followed by either the Heyrovsky step (H
2O + H
ad + e
– ↔ H
2 + OH
−) or the Tafel recombination step (2H
ad ↔ H
2). The detailed mechanism or reaction path is dependent on the components of metal.
Figure 2. (a) Illustration of conventional water electrolyzers. (b) Water-splitting reactions under acidic and alkaline conditions.
Table 2. Summary of typical single-atom metal/2D MoS2 hybrid nanomaterials for water splitting.
Catalyst
|
Electrolyte
|
η (mV)/Best Ratio (w.t.% or Concentration)
|
Tafel Slope (mV dec −1)
|
Stability Test
|
Ref.
|
Co/2D MoS2
|
0.5 M H2SO4
|
42/3.5% Co/1T-MoS2
|
32
|
10,000 CVs
|
[64]
|
Pt/2D MoS2
|
0.1 M H2SO4
|
60/1.5% Pt/MoS2
|
96
|
5000 CVs
|
[20]
|
Pd/2D MoS2
|
0.5 M H2SO4
|
89/1% Pd/1T-MoS2
|
62
|
5000 CVs
|
[65]
|
Ni/2D MoS2
|
0.5 M H2SO4
|
98/Ni/MoS2
|
103
|
2000 CVs
|
[66]
|
Ru/2D MoS2
|
0.5 M H2SO4
|
114/46 μg cm−2 Ru/MoS2
|
-
|
10 h
|
[67]
|
Cu/2D MoS2
|
0.5 M H2SO4
|
131/1% Cu/MoS2
|
51
|
7 h
|
[54]
|
Fe, Co, Ni, Pd, Pt/2D MoS2
|
0.5 M H2SO4
|
140/2.7% Pd/1T-MoS2
|
57
|
1000 CVs
|
[68]
|
Ni/2D MoS2
|
0.5 M H2SO4
|
174/1% Ni/MoS2
|
69
|
1000 CVs
|
[69]
|
Au, Pt, Pd/2D MoS2
|
0.5 M H2SO4
|
210/1.1% Pt/MoS2
|
104
|
5 h
|
[70]
|
Ni/2D MoS2
|
0.5 M H2SO4
|
263/2.7% Ni/MoS2
|
81
|
1000 CVs
|
[71]
|
Ru/2D MoS2
|
1.0 M PBS
|
125/46 μg cm−2 Ru/MoS2
|
-
|
10 h
|
[67]
|
Ru/2D MoS2
|
1.0 M KOH
|
41/46 μg cm−2 Ru/MoS2
|
114
|
20 h
|
[67]
|
Ir/2D MoS2
|
1.0 M KOH
|
44/Ir/1T-MoS2
|
32
|
9000 CVs
|
[72]
|
Ni/2D MoS2
|
1.0 M KOH
|
110/Ni/MoS2
|
119
|
2000 CVs
|
[66]
|
Note: overpotential value (η) and stability test were performed at the current density of 10 mA cm−2; CVs, cycles.