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Single Atom Catalysts for Fuel Cells and
Rechargeable Batteries: Principles, Advances,
and Opportunities
Yuchao Wang,
§
Fulu Chu,
§
Jian Zeng, Qijun Wang, Tuoya Naren, Yueyang Li, Yi Cheng,
Yongpeng Lei,*and Feixiang Wu*
Cite This: ACS Nano 2021, 15, 210−239
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ABSTRACT: Owing to the energy crisis and environmental
pollution, developing efficient and robust electrochemical
energy storage (or conversion) systems is urgently needed but
still very challenging. Next-generation electrochemical energy
storage and conversion devices, mainly including fuel cells,
metal-air batteries, metal-sulfur batteries, and metal-ion
batteries, have been viewed as promising candidates for future
large-scale energy applications. All these systems are operated
through one type of chemical conversion mechanism, which is
currently limited by poor reaction kinetics. Single atom
catalysts (SACs) perform maximum atom efficiency and well-defined active sites. They have been employed as electrode
components to enhance the redox kinetics and adjust the interactions at the reaction interface, boosting device performance.
In this Review, we briefly summarize the related background knowledge, motivation and working principle toward next-
generation electrochemical energy storage (or conversion) devices, including fuel cells, Zn-air batteries, Al-air batteries, Li-air
batteries, Li-CO2batteries, Li-S batteries, and Na-S batteries. While pointing out the remaining challenges in each system, we
clarify the importance of SACs to solve these development bottlenecks. Then, we further explore the working principle and
current progress of SACs in various device systems. Finally, future opportunities and perspectives of SACs in next-generation
electrochemical energy storage and conversion devices are discussed.
KEYWORDS: single atom catalysts, fuel cell, rechargeable battery, electrode, conversion reaction, coordination configuration,
energy storage and conversion, high energy density
INTRODUCTION
Lithium-ion (Li-ion) batteries have been widely used in civil
applications, including mobile communication, transportation,
power storage, aerospace, as well as navigation. However, the
energy densities of commercial Li-ion batteries using Ni/Co-
based cathodes and graphite anodes meet their bottlenecks due
to the limited specific capacities of electrode active materials.
1,2
In the meantime, the battery market is still expanding and
demands lighter and thinner batteries for smart applications. In
recent years, the fuel cells with ultrahigh energy densities have
been viewed as promising candidates for future energy
conversion systems. Especially for electric vehicles (EVs), the
combination employment of fuel cells and Li-ion batteries can
realize the long-lasting and high-power performance. In
addition, rechargeable batteries with potentially high energy
densities have also attracted lots of research efforts.
With the increase of energy consumption and the
appearance of the energy crisis, boosting promising energy
storage and conversion systems with excellent performance
and stability is essential and pressing. Thus, next-generation
energy systems including fuel cells, metal-gas batteries, metal-
sulfur batteries, and metal-ion batteries are widely desirable.
3,4
Nevertheless, these energy storage (or conversion) systems
based on multiple-electron transfer reactions have remained
challenges that hinder their developments and eventual
commercialization.
5,6
For example, both the oxygen reduction
Received: October 16, 2020
Accepted: December 30, 2020
Published: January 6, 2021
Review
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reaction (ORR) and oxygen evolution reaction (OER)
undoubtedly suffer from the sluggish reaction kinetics and
large voltage hysteresis that severely cause rather poor energy
efficiency and low capacity utilization.
7,8
Regarding metal-
sulfur batteries, the shuttle effects of dissolved polysulfides
worsen the reaction interface and cause the loss of active
materials, resulting in short cycle life.
9,10
More importantly, the
conversion reactions among alkali metal sulfides are limited by
poor reaction kinetics, which leads to low capacity utilization
of sulfur, large voltage hysteresis, and unsatisfactory energy
densities.
11
As is known, catalysts provide alternative pathways with
lower activation energy barriers to promote the chemical
reactions.
12-15
So far, homogeneous catalysts and heteroge-
neous catalysts have been employed to accelerate the redox
kinetics in energy storage and conversion systems.
16,17
Owing
to the high price and resource scarcity of precious metals, their
large-scale applications (Pt-based catalysts for ORR and Ru/Ir-
based catalysts for OER) are obstructed. Nonprecious metal
materials serve as the hopeful candidates of precious metals,
but facing low catalytic capability.
18-21
To reduce the usage of
precious metals and further increase the intrinsic activity of
metal atoms, single atom catalysts (SACs) have emerged and
received extensive attention.
22,23
Compared to catalysts in the
nanoscale, the SACs separate their active sites in the form of
single atoms (SAs) without forming nanoparticles or clusters.
Theoretically, SACs ensure the 100% atomic utilization
efficiency, which is extremely valuable for saving metal
resources, especially for precious metals. Through the strong
metal−support interactions, the SAs are anchored on supports
via chemical coordination.
24
Such strong chemical bonding not
only maintains the stability of central atoms, but also acts as a
bridge for charge transfer.
25−27
Moreover, due to their similar
chemical environment and quantized orbital distribution, SACs
show improved reactive selectivity.
28
The applications of SACs
in energy-related devices effectively reduce the metal
consumption and cost and simultaneously keep very small
amounts of catalyst in electrodes while maintaining the
required electrode active mass loadings for achieving high
energy output.
29−31
As shown in Figure 1, various SACs have been successfully
elaborated in fuel cells, metal-air batteries, metal-CO2batteries,
and metal-sulfur batteries, promoting their development. In the
present contribution, we introduce the working principles of
various electrochemical energy storage (or conversion)
systems as well as their remaining limitations that could be
solved via SACs. In turn, the synthesis, tailored configurations,
function designs, and characterizations of SACs have been
presented to guide the future construction of SACs. Moreover,
according to available literature, the reported working
principles of SACs in advanced fuel cells and batteries are
discussed in detail. In the conclusion section, we compare the
Figure 1. SACs and their potential functions in next-generation electrochemical energy storage or conversion devices.
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output properties of reported SAC-based cells/batteries to
acquire a general understanding of the research level. Finally,
the opportunities and perspectives of future efforts that mainly
concentrate on electrode materials and battery structures are
proposed.
ADVANCED FUEL CELLS AND RECHARGEABLE
BATTERIES
As next-generation electrochemical energy storage and
conversion systems, fuel cells and rechargeable batteries
(metal-air batteries, metal-CO2batteries, and metal-sulfur
batteries) display the advantages of large theoretical energy
density, low cost, sustainability, and environmental friend-
liness.
32,33
Fuel cells, being substitutes for internal combustion
engines, point out the direction of electric vehicle energy.
Moreover,wehavesummarizedthetheoreticalenergy
densities (in both gravimetric and volumetric) of different
batteries (Figure 2). Zn-air batteries not only offer the largest
volumetric energy density, but also demonstrate advantages
such as rechargeability and direct utilization of air.
34
The large
volumetric energy density is of great significance to wearable
devices. As for other metal-gas batteries, the direct utilization
of high-capacity alkali metals (Li) is beneficial to reduce the
overall weight of the batteries and increase gravimetric energy
density.
35
The charge and discharge processes of metal-sulfur
batteries depend on the conversion between elemental sulfur
and metal sulfides.
36−39
During the discharge process, multiple
discharge plateaus will appear, corresponding to metal sulfides
with different stoichiometric ratios.
40−43
To fully understand
the basic mechanism and intrinsic challenges of metal-sulfur
batteries, the Li-S and Na-S batteries are chosen for detailed
Figure 2. Theoretical gravimetric/volumetric energy density of various batteries. The data were obtained from refs 34,39,62−64, and 86.
Figure 3. Operation principles of advanced fuel cells and rechargeable batteries.
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discussions, while other metal-sulfur batteries are yet in their
infancy.
44−50
Here, detailed descriptions about operating principles and
features of the above-mentioned batteries will be discussed
separately. Especially, the challenges that can be effectively
solved by catalysts in each battery system are analyzed in detail
in this section.
Fuel Cells. Owing to the advantages of high energy
efficiency, large power density, and quick start, the acidic
polymer electrolyte membrane fuel cells (PEMFCs) have been
widely applied since the 1980s.
51
As the commonly used
PEMFCs, hydrogen oxygen (H2−O2) fuel cells can be seen as
atomically equivalent to the “reverse”devices for water
electrolysis.
52
The unit cell is composed of an anode, a
cathode, and a proton exchange membrane. The H2molecules
are oxidized at the anode side, while the cathode provides a
place in which O2molecules are reduced (Figure 3a). The
ORR process could be divided into two distinct pathways:
efficient 4e−transfer (O2+4H
++4e
−→2H2O) and
inefficient 2e−transfer (O2+2H
++2e
−→H2O2).
53
Briefly,
the 4e−process represents that O2gets 4e−directly then
generates H2O. The 2e−pathway refers to the process in which
O2obtains 2e−to generate H2O2. It is worth noting that the
peroxide ions play harmful effects on ORR which lead to low
efficiency.
54
Hence, the high selectivity for ORR catalysts
toward 4e−transfer pathway is critical on practical occasions.
Compared to the oxidation of H2, the cathodic ORR is the
rate-determining step to control the energy efficiency of fuel
cells. The robust and efficient catalysts are required to catalyze
the cathode reaction. For other fuel cells that use organic fuels
as anode active materials, the demands for catalyzing anode
conversion are also urgent. Thus, bifunctional catalysts, which
can simultaneously achieve the reduction of O2and the
oxidation of anode fuels, are also required.
Zn-Air Batteries. Rechargeable Zn-air batteries possessing
high specific energy and volumetric energy density have a great
promise in portable equipment.
55−58
Owing to the employ-
ment of aqueous or solid electrolytes, Zn-air batteries have
advantages in terms of safety and portability. As shown in
Figure 3b, metal Zn serves as the negative electrode active
substance while O2acts as the positive electrode active
material. During the discharge process, electrons are released
from the Zn electrode to the air electrode and the Zn atoms
are oxidized into Zn2+ ions. Meanwhile, O2diffuses into the air
electrode and is reduced into OH−ions via the ORR route (O2
+2H
2O+4e
−→4OH−).
59,60
Then, the OH−ions migrate
around the Zn electrode and combine with Zn2+ ions to form
zincate ions (Zn(OH)42−) that would be decomposed into
ZnO under supersaturated concentrations (Zn + 2OH−→
ZnO + H2O+2e
−).
61
During the charge process, Zn-air
batteries convert electrical energy into chemical energy
through OER. The OH−ions are oxidized to generate O2
(4OH−→O2+2H
2O+4e
−).
62,63
The overall charge−
discharge processes can be summarized into the reversible
reaction (2Zn + O2⇔2ZnO) (Figure 3b).
64,65
However, Zn-
air batteries are suffering from short operating lifetimes and
Figure 4. Typical charge and discharge curves. (a) Li-air batteries. Adapted with permission from ref 5. Copyright 2020 The Royal Society of
Chemistry. (b) Li-CO2batteries. Adapted with permission from ref 78. Copyright 2017 Elsevier. (c) Li-S batteries. Adapted with permission
from ref 39. Copyright 2016 The Royal Society of Chemistry. (d) Na-S batteries. Adapted with permission from ref 107. Copyright 2015
Wiley-VCH.
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low energy conversion efficiency that are mainly due to the
inherently slow kinetics of the ORR/OER and the poor
stability of air electrodes in corrosive electrolytes.
66−68
Therefore, efforts are being made to develop durable and
nonprecious metal ORR/OER catalysts.
69
Al-Air Batteries. Al-air batteries are made of high-purity Al
or Al alloy as anodes, O2(air) electrode as cathodes, and alkalis
or salts as electrolytes. During the discharge process, the anode
materials dissolve and the O2molecules are reduced to release
electrical energy, which is similar to the working principle of
Zn-air batteries. The overall reaction can be described as
follow: Al + 3/4O2+ 3/2H2O→Al(OH)3.
70
However,
thermodynamic limitation makes it hard to process the
reduction of Al(OH)3during charging. The deposition of Al
electrode requires very negative potentials in an aqueous
system, which cause intense H2evolution prior to Al
deposition.
71
Therefore, the rechargeability of Al-air batteries
is challenging. The catalytic sites with high intrinsic ORR
activity are expected to enable the fast kinetics and mass
transfer at the three-phase interface.
Li-Air Batteries. Li-air batteries employ metal Li as
negative electrodes, O2as positive electrode reactants and
nonaqueous solutions as electrolytes (Li-air batteries based on
alkali aqueous electrolytes are omitted in this Review). During
the discharge process, the ORR occurs at the cathode. The
metal Li anode dissolves and passes through the electrolytes to
react with O2, forming Li2O2or Li2O. For the charge process,
the Li2O2(or Li2O) decomposes into metal Li and O2, which
is the OER process (Figure 3c). The entire cycle can be
described as 2Li + O2⇔Li2O2or 4Li + O2⇔2Li2O.
72−74
In theory, the specific energy of Li-air batteries is higher than
those of other metal-air batteries.
75
But the kinetic problems in
Li-air batteries are serious. On one hand, the reactivity of metal
Li places severe requirements on the design of battery
structures. The direct contact between metal Li and H2O/air
should be prohibited. On the other hand, the slow kinetics
issues coming from the generation and decomposition of
Li2O2/Li2O reduce the round-trip efficiency (Figure 4a). In
particular, the decomposition of solid-state discharge products
is rather difficult, ultimately causing the large overpotential,
low rate capability and poor cycling efficiency of Li-air
batteries.
76
Exploring porous cathode catalysts to regulate the
growth and decomposition of solid-state discharge products is
of practical significance.
Li-CO2Batteries. Metal-CO2batteries are not only efficient
energy supply systems but also helpful to achieve CO2fixation
and carbon neutral cycle.
77
Importantly, the research and
application of metal-CO2batteries will play a role in Mars
explorations due to the extremely high CO2content (over
95%) in the Mars atmosphere. Among the known metal-CO2
batteries, Li-CO2batteries demonstrate the largest theoretical
energy density. They adopt metal Li as anode materials, while
the CO2molecules are chosen as cathode reactants and energy
carriers.
78
The formation and decomposition of Li2CO3(4Li +
3CO2⇔2Li2CO3+ C) during the discharge/charge process
happens. In the discharge process, Li ions are released to the
gas electrode and react with CO2to produce Li2CO3
precipitates (Figure 3d). The large surface area of gas electrode
is required to accommodate these discharge products. In order
to achieve the decomposition of Li2CO3, the charging process
often requires an overpotential above 4 V. Such a high charging
voltage not only results in the loss of energy efficiency, but also
possibly causes the decomposition of organic electrolytes.
79,80
Therefore, the slow formation and decomposition of metal
carbonates restricts the development of metal-CO2batteries
(Figure 4b).
81
Gas electrode catalysts that promote the
decomposition of Li2CO3are currently the main research
content in Li-CO2batteries.
Li-S Batteries. Lithium-sulfur (Li-S) batteries using high-
capacity sulfur and Li as electrode active materials can deliver a
high theoretical energy density (Figure 3e). Moreover,
considering the lower economic cost and environmental
friendliness of earth-abundant sulfur, Li-S batteries have been
viewed as a promising candidate in the field of future
batteries.
82
As it is well-known, the conversion reaction in
Li-S batteries can be summarized by the equation 16Li + S8→
8Li2S.
83−85
However, the discharge process is complicated and
involves multiple steps as presented in Figure 4c. It mainly
includes two steps (two visible plateaus in the discharge curve
in Figure 4c) according to solid-to-liquid (S8→Li2S8→Li2S6
→Li2S4) and liquid-to-solid (Li2S4→Li2S2→Li2S) phase
transformations. More precisely, the most challenging issue in
Li-S batteries is the shuttling effect that stems from the former
intermediates: highly soluble long-chain polysulfides (Li2S8,
Li2S6, and Li2S4) in most organic liquid electrolytes. This
unwanted shuttle between the Li metal and sulfur cathode
during the discharge−charge process worsens the reaction
interface, leading to increased internal resistance and capacity
loss with cycles. Moreover, as the discharge products, both
Li2S2and Li2S are natural insulators, causing the poor reaction
kinetics of the conversion reaction between Li2S2and Li2S.
This limited solid-to-solid conversion reaction largely reduces
the capacity utilization of sulfide cathode, rate performance,
energy efficiency, and the final practical energy densities. In the
charge process, the activation of Li2S needs a visible charge-
overpotential that is the high energy barrier of Li extraction to
overcome. By feat of strategies based on physical or chemical
methodologies, the shuttle effect of polysulfides in Li-S
batteries has been partly alleviated so far.
86
Physical confine-
ment availing of carbonaceous materials, such as graphene,
87
mesoporous carbon,
88
and metal−organic frameworks,
89
can
wrap up polysulfides in pores or block them by interlayer
spaces. Meanwhile, chemical bonding with polysulfides by
effective heteroatom dopants in a substrate can strengthen the
interaction to further eliminate the detrimental shuttle
effects.
90,91
In addition, the chemical interactions can
compensate for the unavoidable out-diffuse of polysulfides
during extended cycles, as the binding force between nonpolar
carbon and polarized polysulfides is so insufficient.
92,93
The metallic Li anodes display severe challenges of side
reactions caused by high reactivity of Li.
94
As a result, various
components in the electrolyte system could induce the
interfacial layer on Li anodes with ion conduction but no
electron conduction, the so-called solid electrolyte interphase
(SEI).
95
However, the repeated Li plating/stripping behavior
can lead to the undesired fracture and growth of the SEI layer,
which causes rather thick SEI layer, continuous consumption
of both active lithium and electrolyte in parasitic reactions, as
well as low Coulombic efficiency (CE). Furthermore, the
irregular Li deposition and preferred orientation growth of
microcrystal easily generated lithium dendrites, resulting in
early failure and security problems.
96
When meeting tougher
conditions (to achieve practical high energy densities in Li-S
batteries), such as high sulfur loading, high rate discharging, or
lean electrolyte condition (low electrolyte/sulfur ratio), the
above issues in Li-S chemistry are becoming even worse. For
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example, the conversion reaction in rather thick S electrodes
will suffer from more sluggish kinetics, resulting in lower
capacity utilization.
97,98
Therefore, designing efficient catalysts
would be an effective and indispensable strategy to regulate the
performance of Li-S batteries via promoting fast conversion of
sulfur species, efficient trapping of polysulfides, and uniform
lithium nucleation.
Na-S batteries. Considering the large abundance and low
cost of Na, Na-S batteries with potentially high energy density
are capable of the adaptation of large-scale energy storage and
even EVs in the future.
99,100
Since the 1960s, according to the
history of Na-S batteries, high-temperature sodium-sulfur (Na-
S@HT) batteries took the lead in realizing commercialization
in the stationary energy storage field, in which molten sulfur
coupled with sodium beta-alumina (β-NaAl11O17) served as an
efficient solid-state Na-ion conductor.
101,102
However, owing
to the rather high operating temperatures at 300−350 °C, the
potential security risks and extra maintenance expenditure have
made conventional Na-S@HT batteries impossible to be
employed for EVs. Since 2012, plenty of research efforts have
been conducted to develop room-temperature sodium-sulfur
(Na-S@RT) batteries for future practical applications.
103,104
Compared to Li-S conversion chemistry, Na-S@RT batteries
display more serious issues caused by polysulfides shuttle
effects, sluggish reaction kinetics, and Na dendrites. As a
consequence, the low efficiency, low capacity utilization and
fast capacity degradation during cycling indeed impeded
commercial development of Na-S@RT batteries, which
currently cannot compete with the cycling lifespan (2500
cycles) achieved in Na-S@HT batteries.
105,106
According to
the available literature,
103,104
the conversion reaction chemistry
in Na-S@RT batteries can be summarized in the following
equations (Figure 3f):
Figure 5. Synthesis, characterization and property of SACs. Wet chemical method. Adapted with permission from ref 110. Copyright 2018
American Chemical Society. ALD method. Adapted with permission under a Creative Commons CC BY License from ref 112. Copyright
2020 Nature Publishing Group. Electrochemical etching method. Adapted with permission under a Creative Commons CC BY License from
ref 113. Copyright 2019 Nature Publishing Group. Ball-milling process. Adapted with permission from ref 115. Copyright 2020 American
Chemical Society. High-temperature atom trapping method. Adapted with permission from ref 116. Copyright 2020 Wiley-VCH. Host−
guest strategy. Adapted with permission from ref 118. Copyright 2017 American Chemical Society. Ligand-assisted method. Adapted with
permission under a Creative Commons CC BY License from ref 148. Copyright 2018 Nature Publishing Group. Solid-phase thermal
diffusion method. Adapted with permission under a Creative Commons CC BY License from ref 160. Copyright 2019 Nature Publishing
Group. Electrodeposition method. Adapted with permission from ref 168. Copyright 2020 The Royal Society of Chemistry.
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During the discharge process in Na-S@RT batteries, the
coexistence and interconversion of various polysulfide
substances (Na2Sn,4≤n≤8) will persistently occur in the
most complicated region II (Figure 4d). What is worse,
subsequent electrochemical reactions are usually not complete,
especially in region IV as the deficient conductive property of
solid Na2S2and Na2S.
107
The slow reaction kinetics and high
polarization significantly affect the overall discharge perform-
ance. Thus, parts of the discharge reaction are disappeared. In
the opposite process, the utilization of active S-species would
be further decreased during the charge process. Meanwhile,
similar to the case of the metallic Li anode, the uneven Na
deposition, unsubstantial interfacial layer, and further dendritic
growth during cycling require special attention to be controlled
as well. Hence, to realize successful applications of Na-S@RT
battery, more significant progress should be made to enhance
the reaction kinetics and cycle stability in Na-S battery, as well
as to comprehensively understand the Na-S conversion
reaction mechanism. Only then would Na-S@RT batteries
be an absolute option on account of low cost and reasonable
energy density.
Obviously, toward diverse battery systems, although
potential progress has been made, the research bottlenecks
of critical catalytic reactions still seriously exist. Such
challenges make their output performance far from the
theoretical level. As a promising part of battery construction,
applying SACs in electrode materials represents a research
direction which could narrow the gaps between practical
applications and theoretical level to a certain extent.
SYNTHESIS AND CHARACTERIZATION OF SACs
In order to meet the demand for highly active catalysts in
various catalytic situations, many synthesis strategies toward
SACs have been developed. In general, the “bottom-up”and
“top-down”methods are common strategies (Figure 5).
108
For
the former, the wet chemical methods consisting of wet-
impregnation and coprecipitation perform the advantages of
simple operation and scale preparation.
109,110
However, the
subsequent reduction treatments, such as H2reduction and
photochemical reduction, are necessary. The produced
catalysts usually demonstrate shortcomings of low metal
loading and agglomeration.
111
Requiring complicated equip-
ment, atomic layer deposition (ALD) method further improves
the productivity and controllability, while the precise control of
film thickness can be achieved.
112
In addition, electrochemical
deposition and chemical vapor deposition have been reported
to prepare SACs.
113,114
As one of the top-down methods, the ball-milling is
relatively simple to realize large-scale preparation.
115
The
high-temperature atomic trapping,
116
solid phase thermal
diffusion
117
and the pyrolysis of metal organic complexes
also receive attention. The pyrolysis of metal organic
complexes typically employs various precursors with features
of molecular confinement and organic ligand coordination.
And the pyrolysis procedure greatly improves the stability of
metal SAs, which is conducive to increasing metal loading and
enhancing catalytic durability.
118
It is worth noting that these
complex precursor-based pyrolysis strategies produced uni-
formly dispersed M−N−C sites, which are regarded as the
most hopeful nonprecious metal-based ORR catalysts.
119
Thus,
although consuming organic reagents, the top-down methods
display obvious advantages over those bottom-up methods.
Very recently, some meaningful strategies were also reported.
For instance, a shockwave synthesis method anchored SAs on
carbon supports, which could remain stable under a high
temperature.
120
Also, a universal precursor-dilution strategy
utilized the chelation between porphyrin molecules and metal
cations to prepare 24 different SACs.
121
Diversified synthetic
strategies bring more opportunities for coordination config-
uration regulation and catalytic activity promotion.
In addition to the advancement of synthetic methods, the
development of SACs is also closely related to the progress of
characterization technologies. The aberration-corrected high-
angle annular dark-field scanning transmission electron
microscopy (AC HAADF-STEM) and synchrotron-based X-
ray absorption spectroscopy (XAS) are most effective
characterization tools in connection with SACs. At present,
the HAADF-STEM is the only tool that can directly observe
SAs via the brightness difference among different elements.
The local information and spatial dispersion of atoms are
presented.
122
The XAS can be divided into X-ray absorption
near-edge structure (XANES) spectra and extended X-ray
absorption fine structure (EXAFS).
123
The XANES is sensitive
to the oxidation states of atoms, while the EXAFS is sensitive
to the coordination distances, coordination species and
coordination numbers. Therefore, the local electronic structure
and chemical environment of the central atoms can be realized
at atomic scale.
124
On the basis of experimental information,
the reasonable structural model can be established for
theoretical study. As a special advantage of SACs, the
homogeneously dispersed and separated active sites provide
a great convenience for density functional theory (DFT)
calculations. It is worth mentioning that some of recent articles
have pointed out the reconstruction of catalysts during
reaction process. Hence, to figure out the real active species
and clarify the reaction mechanism, in situ technologies
Figure 6. Development history of SACs in fuel cells and batteries.
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(Raman spectrum, XANES, EXAFS, infrared spectrum, etc.)
are required.
125
Benefiting from the improvements in synthesis methods and
advancements in characterization technologies, the modulation
and recognition of coordination structure toward SACs
achieved significant progress, which pushed their applications
in the energy field. Here, we set our sights on SAC-based
electrode materials for advanced fuel cells and batteries. The
related parameters to evaluate device performance (cycle life,
energy density, etc.) are also presented (Figure 5).
ADVANCES OF SACs IN FUEL CELLS AND
RECHARGEABLE BATTERIES
Dispersed M−N−C active centers have received great
attention.
126
Among different transition metals, Fe-based
SACs have been extensively studied due to their high ORR
intrinsic activity and no toxicity. The timeline of SACs in fuel
cells and batteries is shown in Figure 6. SACs have been
employed to develop Zn-air batteries since 2017. Then, they
were also chosen in PEMFCs, Li-S, and Na-S chemistries to
drive the energy devices toward high output, great portability,
environmental friendliness, and low cost. Very recently, SACs
have been used in Al-air, Li-CO2, and Li-air batteries.
SACs in PEMFCs. Since Pt-based catalysts have been
largely used in PEMFC cathode, improving the Pt utilization
and developing non-Pt catalysts is urgent and necessary.
127
Xu
et al.
128
simultaneously anchored Pt SAs and nanoparticles on
defective carbon supports. The Pt1.1/BPdefect-based PEMFCs
achieved a power density of 520 mW cm−2,which
corresponded to the Pt utilization of up to 0.09 gPt kW−1.
Shui et al.
129
prepared a series of precious metal SAs (Pt, Pd, Ir,
Rh) on ZIF-derived carbon. They proposed that the
electronegativity of coordinated anions should match with
the OH*absorbance ability of precious metal atoms to
enhance ORR activity. The atomically dispersed metal atoms
anchored on carbons are potential to replace their particle/
cluster counterparts.
130
Figure 7. SACs in PEMFCs. (a) Discharge polarization curves and power density plots. Reprinted with permission from ref 132. Copyright
2020 Wiley-VCH. (b) Stability curves. Reprinted with permission under a Creative Commons CC BY License from ref 135. Copyright 2019
Wiley-VCH. (c) Discharge curve at a constant potential. Reprinted with permission from ref 136. Copyright 2019 The Royal Society of
Chemistry. (d) Fe k-edge fittings curves and the structural model of FeNi−N6. Reprinted with permission from ref 137. Copyright 2020
American Chemical Society. (e) Polarization and power density curves. (f) Correlation between active site densities and power density.
Reprinted with permission from ref 140. Copyright 2019 Elsevier.
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Under real operating conditions, the slow mass transfer
process would cause the accumulation of products and
insufficient supply of reactants, which subsequently affects
the output performance of fuel cells.
131
To alleviate this
problem, Wang and co-workers
132
constructed hierarchical
ordered porous carbon as a skeleton to accommodate Fe−N4
active sites. The resulting PEMFCs exhibited an open circuit
voltage (OCV) of 0.98 V and maximum power density of 0.42
Wcm
−2under 1 bar H2/air (Figure 7a). This hierarchical
ordered porous structure had a significant improvement in the
mass transfer process, which was also proved by the work of
Liao et al.
133
Shui et al.
134
manufactured concave-morphology
Fe−N−C SACs (TPI@Z8(SiO2)-650-C) with 10 nm thin
layer to promote mass transfer. The SiO2coating with ZIF-8
played crucial roles in the formation of concave shape. The
proportional relationship between current density and active
site density proved the contribution of Fe−N−C sites to
catalytic activity. Thus, increasing active site density is a
reliable measurement to promote performance.
Aiming to resist the corrosion of electrode materials under
acidic conditions, Cheng et al.
135
developed FeSA-G with high
metal loading up to 7.7 wt % to meet the high temperature
operation and phosphate corrosion environments. In high
temperature phosphoric acid/polybenzimidazole (PA/PBI)
composite membrane fuel cells using FeSA-G as the cathode,
a power density of 325 mW cm−2was obtained at 230 °C,
which exceeded that of its counterparts using Pt/C (313 mW
cm−2). Under a cell voltage of 0.6 V, the polarization curves of
PEMFCs were stable at 230 °C for 100 h. No obvious
structural change was observed (Figure 7b). Wu and co-
workers
136
prepared 1.5Fe-ZIF and explored the reasons for
their performance degradation in acidic conditions. The 1.5Fe-
ZIF based PEMFCs were subjected to constant-potential
testing at 0.85 V in 0.5 M H2SO4until 100 h (Figure 7c).
Obviously, the catalytic current density was reduced to 30% of
the initial value. Due to the carbon corrosion, the N−C and
Fe−N bonding became weak and broken while the Fe clusters
appeared. Hence, the durability of Fe−N−C sites in acidic
conditions was still an extremely hard challenge.
The multisite structure could promote the formation of O−
O bridge models, which is beneficial to boost the O−O bond
breakage and 4e−reduction reaction. Therefore, Sun et al.
137
introduced Ni−Nxinto Fe−N−C species to reduce the
adsorption of H2O2. Quantitative XANES fitting indicated
that a Fe−N4configuration combined with a Ni−N4
configuration to form a FeNi−N6motif rather than M−N3
sites (Figure 7d). Compared to single Fe−N4sites, FeNi−N6
displayed better ORR activity, turnover frequency (TOF), 4e−
selectivity, stability, and methanol resistance. In PEMFCs using
FeNi−N6as a cathode, the initial maximum power density
reached 216 mW cm−2under the H2/O2condition. Due to the
coexistence of Ce3+ and Ce4+, ceria can release or store O well,
thus promoting the O2adsorption and occurrence of the ORR
process. Shao and co-workers
138
developed active Fe−N−C
sites (Ce/Fe-NCNW), in which the Fe SAs coordinated not
only with 4 N atoms but also with the 1 O atom of ceria.
Under the H2/O2condition with a pressure of 30 psi, the
power density of PEMFCs attained 496 mW cm−2. So, the
advantage of special oxides over carbon-based supports cannot
be ignored.
The Fenton reaction, during which Fe2+ mixes with H2O2to
oxidize organic compounds, eventually causes damage to the
polymer membrane and affects the stability of fuel cells.
139
Although Fe−N−C species show great ORR property, it also
makes sense to develop other SACs to avoid the harmful
Fenton reaction. Shui et al.
140
utilized an electrochemical
method to control the density of CoN4. As the weight ratio of
cobalt acetate in precursor increased to 1.6, the 1.6%CoNC-
ArNH3catalyzed PEMFCs emerged the largest power density
of 826 mW cm−2under the pressure of 2.5 bar H2/O2(Figure
7e). Further increase of Co content caused the formation of
nanoparticles, which was not conducive to the occurrence of
ORR (Figure 7f). In addition, the utilization of Mn−N−Cin
fuel cells also effectively avoided the Fenton reaction. Wu et
al.
141
discovered that the doped Mn in carbon mixture
probably enhanced the degree of graphitization, which was
beneficial to improving the corrosion resistance of carbon
materials. In 0.5 M H2SO4, the 20Mn-NC-second endured
3000 cyclic voltammetry (CV) cycles with minor loss of half-
wave potential (E1/2). Then, at a constant potential of 0.8 V,
the 20Mn-NC-second possessed smaller current density decay
than 20Fe-NC-second, indicating the predominant carbon
corrosion resistance toward Mn-based active sites.
Table 1. Summary of SACs in PEMFCs
catalysts configuration power density (mW cm−2) open circuit voltage (V) stability refs
Ir1-N/C Ir−N4870(O2)/380(air) 0.95(O2)/0.93(air) 50 h 129
Co@SACo-N-C Co−Nx420(O2)/230(air) 0.91(O2)/0.91(air) 10 h 131
FeN4/HOPC-c-1000 Fe−N4660(O2)/420(air) 0.99(O2)/0.91(air) 100 h 132
C-FeHZ8@g-C3N4-950 Fe−N4628(O2) 0.98(O2)8h133
TPI@Z8(SiO2)-650-C Fe−N4420(air) 0.91(air) 134
FeSA-G Fe−N4325(O2)
a
0.9(O2)
a
100 h 135
1.5Fe-ZIF Fe−N4660(O2)/360(air) 0.98(O2)/0.95(air) 100 h 136
FeNi-N6FeNi-N6216(O2) 0.82(O2)137
Ce/Fe-NCNW Fe−N4-O 496(O2)
b
1.02(O2)
b
138
20Co-NC-1100 Co−N4560(O2)/280(air) 0.95(O2)/0.89(air) 100 h 139
CoNC-ArNH3Co−N4440(O2)/221(air)
c
0.88(air)
c
20 h 140
20Mn-NC-second Mn−N4460(O2) 0.95(O2) 100 h 141
Fe−C−N950 680(O2) 0.80(O2)143
Fe SAs/N−CFe−N4680(O2)/350(air) 0.83(O2)/0.89(air) 145
Fe-SAs/NPS-HC Fe−N4333(air) 0.96(air) 148
SA-Rh/CN Rh−N/O 522.1 mW mg−10.77 50 000 s 142
a
Test under 230 °C.
b
Test under 30 psi.
c
Test under the pressure of 0.5 bar.
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Considering that the PEMFCs have high operating temper-
atures (up to 200 °C) and acidic working conditions, the
serious corrosion to carbon-based supports will bring
challenges to the practice of SACs. Table 1 summarizes the
recent PEMFCs using SACs as cathodes. Under H2/O2and
H2/air conditions, the power density and OCVs of PEMFCs
are obviously different. Such declining performance under H2/
air atmosphere suggests that sufficient mass transfer influences
integral output performance. Apart from the intrinsic ORR
property of catalysts, developing diverse metal centers,
optimizing morphology structure to accelerate mass transfer
and designing reasonable component to enhance durability
should also be considered.
Although achievements of SACs in H2−O2fuel cells have
been made, the works toward other PEMFCs, such as direct
formic acid fuel cells (DFAFCs) are rarely reported. Wang and
co-workers
142
employed the SA-Rh/CN for DFAFCs anode
catalysts in which Rh atoms coordinated with 4 N atoms and 2
O atoms. When used for formic acid oxidation, SA-Rh/CN
displayed a mass activity of 16.1 A mg−1and a TOF of 8.55 s−1,
both exceeding those of commercial Pd/C. In DFAFCs, SA-
Rh/CN exhibited mass power densities of 522.1 mW mg−1
(8.8 times of Pd/C) at 30 °C and 1241.9 mW mg−1at 80 °C.
Additionally, the CO adsorption on the SA-Rh/CN surface
was weakened and the dehydration of formic acid was
suppressed, which was also confirmed by DFT calculations.
The high CO production barrier and relatively unfavorable
binding between SA-Rh/CN and CO molecules resulted in
excellent CO tolerance.
SACs in Zn-Air Batteries. Toward ORR for Zn-air
batteries, Fe-based SACs have also attracted a lot of research
efforts. Chen and co-workers
144
developed single Fe atoms
(metal loading of 1.96 wt %) on N-doped porous carbon
(NPC) by an in situ anchor strategy. Carrying a valence
between +2 and +3, each Fe atom coordinated with 4 N atoms
to form Fe−N4active sites that demonstrated O2activation
capacity (Figure 8a). The prepared Fe−N4SAs/NPC
displayed an onset potential (Eonset) of 0.972 V and an E1/2
of 0.885 V in 0.1 M KOH. The corresponding Zn-air batteries
showed a power density of 232 mW cm−2(Figure 8b) without
evident voltage changes after 108 cycles, which were better
than those of the Pt/C+Ir/C-based counterparts. To boost the
power density, Fe SAs (Fe−N4) with metal loading up to 3.8
wt % on crumpled N-doped carbon nanosheets (Fe SAs/N−
C) were developed, yielding an E1/2 of 0.91 V in 0.1 M KOH
(Figure 8c).
145
Correspondingly, the Zn-air batteries achieved
a power density of 225 mW cm−2. DFT calculations showed
that the limiting potential of Fe SAs/N−C reached up to 0.76
V, which was close to that of Pt (0.79 V).
Heteroatom doping in SACs has been widely employed to
improve the conductivity of the carbon matrix and modify the
coordination environment of central atoms.
146
As reported, the
codoped N and S atoms could cause the charge redistribution
in the carbon framework and boost bifunctional ORR/OER
activity of atomically dispersed Fe−Nxsites.
147
Wang et al.
148
synthesized effective Fe SAs anchored on N, P, S codoped
hollow carbon (Fe-SAs/NPS-HC) via the so-called MOF@
polymer strategy. The E1/2 values of 0.912 and 0.791 V were
obtained in 0.1 M KOH and 0.5 M H2SO4, respectively. As
primary active sites, the isolated Fe−N4species activated and
reduced O2. The homogeneously dispersed P and S atoms did
not coordinate with Fe atoms directly but modulated the
electrical states via long-range interactions, which weakened
the binding toward OH*intermediates to release OH−(Figure
Figure 8. Fe-based SACs in Zn-air batteries. (a) EXAFS result. (b) Charge−discharge polarization curves and power density plots. Reprinted
with permission from ref 144. Copyright 2018 Wiley-VCH. (c) LSV curves. Inset: HAADF-STEM image of Fe SAs/N−C. Reprinted with
permission from ref 145. Copyright 2019 American Chemical Society. (d) Linear relationship between OH*binding energy and Bader
charge. (e) Discharge polarization curves and power density plots. Inset: Schematic model of Fe-SAs/NPS-HC. Reprinted with permission
under a Creative Commons CC BY License from ref 148. Copyright 2018 Nature Publishing Group. (f) Gibbs free energy diagrams.
Reprinted with permission from ref 149. Copyright 2020 American Chemical Society.
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8d). The Zn-air batteries displayed an OCV of 1.45 V and a
power density of 195.0 mW cm−2at a current density up to
375 mA cm−2(Figure 8e). Furthermore, the N, P co-
coordinated Fe−N3P configuration showed the lower free
energy of primitive steps than traditional Fe−N4sites, which
was more conducive to the adsorption of O2and the
occurrence of rate-determining step (OH*to OH−)(Figure
8f).
149
Xiang and co-workers
150
coupled the graphene matrix
with covalent organic frameworks (COFs) containing Fe−N4
active species via intermolecular interactions. Apart from the N
atoms in COFs, Fe SAs simultaneously coordinated with C
atoms from graphene. The assembled Zn-air batteries delivered
an OCV of 1.41 V, a power density of 123.43 mW cm−2, and a
long-term stability of over 300 h with voltage attenuated less
than 0.1%. Apart from these, the oxygen dangling bonds on the
graphene oxide (GO) surface could trap metal (Fe, Co, Ni,
Cu) atoms and construct corresponding M−O4sites at room
temperature.
151
The mild and economically friendly synthesis
strategies operated under low temperature effectively reduce
the energy consumption, deserving our attention.
Recently, the Co−N−C sites with good bifunctional ORR/
OER performance have been widely used in rechargeable Zn-
air batteries. Zhang’s group
152
investigated Co-POC SACs
using π−πcongregated porphyrin and graphene as pyrolysis
precursors. In 0.1 M KOH, Co-POC demonstrated an E1/2 of
0.83 V for ORR and a η10 of 470 mV for OER. A low ΔE(the
value between E1/2 and η10) of 0.87 V also proved the
bifunctional ORR/OER performance. They further designed
Co−Nx−C active moieties with the Co loading of 1.23 wt %
for flexible Zn-air batteries (Figure 9a).
153
Applying alkaline
poly(vinyl alcohol) (PVA) gel as an electrolyte, the Zn-air
batteries showed a high OCV of 1.439 V. They also endured
long-term charge/discharge cycles and bending at different
angles without obvious performance changes. In order to
enhance the flexibility and wearability of Zn-air batteries, Guo
et al.
154
reported a bifunctional Co−N4moiety (2.05 wt %) on
electrospun fibers (Co SA@NCF/CNF) as binder-free air
electrodes. An E1/2 of 0.88 V and a η10 of 400 mV were
achieved in 1 M KOH (Figure 9b). The wearable Zn-air
batteries displayed an OCV of 1.41 V and a capacity of 530.17
mAh gZn
−1. They showed higher discharge voltages and more
stable discharge platforms than those of their Pt/C+Ir/C-based
counterparts (Figure 9c). After frequent folds, the batteries can
still work well, displaying the resistance to external pressure
(Figure 9d). The supports possessing rough surfaces, rich
channels, and plentiful pores are beneficial to mass transfer at
the electrochemical interface.
155
Lu et al.
156
combined the
coordination environment regulation and porosity/conductiv-
ity decoration in Co-based SACs. The constructed Co-N3C1-
based Zn-air batteries achieved a peak power density of 255
mW cm−2. The importance of combined electronic state
regulation and morphology optimization was highlighted.
Toward flexible Zn-air batteries, other Co-based SACs were
also constructed.
157−159
Development of central atoms, synergy between multimetal
sites, and design of supports are the strategies currently
involved. Wu and co-workers
160
reported a high-temperature
gas-transport strategy to construct single Cu atoms on N-
doped carbon with rich defects. The Cu SAs, with a valency
between 0 and +2 (Figure 10a), coordinated with 3 N atoms
(Figure 10b). The Cu ISAS/NC-based Zn-air batteries
achieved a power density of 280 mW cm−2and a specific
Figure 9. Co-based SACs in flexible Zn-air batteries. (a) Schematic illustration of the flexible Zn-air batteries. Reprinted with permission
from ref 153. Copyright 2017 Wiley-VCH. (b) ORR/OER bifunctional LSV curves. (c) Discharge curves at different current densities. (d)
Charge−discharge curves after frequent folds. Reprinted with permission from ref 154. Copyright 2019 Wiley-VCH.
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capacity of 736 mAh g−1(Figure 10c). In addition, the Cu SAs
(Cu−N3) have been successfully fixed on hollow N-deficient
carbon nitride nanospheroids (CuSA@HNCNx). Under the
same synthesis conditions, the ORR/OER activities of CuSA@
HNCNxeven surpassed those of FeSA@HNCNxand CoSA@
HNCNx, illustrating the feasibility of Cu-based SACs for air
electrodes (Figure 10d).
161
Mo-based bifunctional catalysts
from the size of nanoparticles to SAs were reported.
162
The
Mo1N1C2active sites achieved the lowest ORR and OER
overpotentials compared to those of the nanoparticle and
cluster counterparts (Figure 10e). Theoretically, Kulkarni and
co-workers
163
selected Cu-modified covalent triazine frame-
works as model SACs (Cu/CTF) and carried out calculations.
Based on the electronic structure analysis and solvation effects,
the appropriate descriptions to evaluate ORR activities were
proposed, which not only discovered the origin of ORR
activity toward Cu/CTF but also can be extended to other
SACs.
By simultaneously introducing multiple metal SAs on
carbon-based supports, the interactions between different
metal atoms may enhance the catalytic property. Jia et al.
164
prepared Fe, Co SA coexisting catalysts with the proximate
configuration of M−N4. According to the free energy path in
theoretical calculations, Fe and Co atoms affected the
electronic structure of each other, which was conducive to
the occurrence of ORR process. In Zn-air batteries, FeCo-IA/
Figure 10. Non-Fe, Co-based SACs in Zn-air batteries. (a) Cu K-edge XANES and (b) EXAFS results. (c) Discharge polarization curves and
power density plots. Reprinted with permission under a Creative Commons CC BY License from ref 160. Copyright 2019 Nature Publishing
Group. (d) ORR/OER bifunctional LSV curves. Reprinted with permission from ref 161. Copyright 2020 Elsevier. (e) ORR/OER
theoretical overpotentials versus adsorption free energies. Inset: Mo1N1C2model. Reprinted with permission from ref 162. Copyright 2020
Elsevier. (f) Discharge polarization curves and power density plots. Inset: SA-PtCoF model. Reprinted with permission from ref 168.
Copyright 2020 The Royal Society of Chemistry.
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NC drove an OCV of 1.472 V and a power density of 115.6
mW cm−2. Ma and co-workers
165
constructed hollow graphene
nanospheres with Fe−N4sites in outer layers and Ni−N4sites
in inner layers. The excellent ORR and OER properties, which,
respectively, originated from Fe−N4and Ni−N4species,
endowed the Zn-air batteries with high energy efficiency and
durability. The metal−support interactions not only stabilize
metal SAs on the supports but also regulate their geometric
environment and electronic structure to enhance the intrinsic
activity.
166
Xu and co-workers
167
deposited Co SAs on Co3O4
particles and N-doped carbon. The interactions among Co
SAs, Co3O4and N-doped carbon enhanced the ORR/OER
activity. Yang’s group
168
built PtCo alloy nanosheets with
interstitial F doping (SA-PtCoF). The F atoms caused the
lattice disorder and weakened the Pt−Co bonds, eventually
generating stable Pt SAs on nanosheet edges. The electrons
transferred from Co to adjacent Pt atoms, pulling down the d-
band center of Pt and adjusting the adsorption behavior of
intermediates. Correspondingly, the electronic structure of Co
was also affected by adjacent Pt atoms, which could promote
the OH−adsorption during OER process. The SA-PtCoF-
based Zn-air batteries gained a power density of 125 mW cm−2
(Figure 10f). Here, the Co supports also acted as active
species, while the Pt SAs served as cocatalysts to a certain
extent.
As a short summary, the Fe−N−C and Co−N−C sites are
the most commonly used active species for cathode materials
of Zn-air batteries (Table 2). Although Fe-based SACs
displayed good ORR performance, the Co-based SACs showed
evident advantages in rechargeable batteries due to their
bifunctional activity. The strategies such as heteroatom doping,
Table 2. Summary of SACs in Zn-Air Batteries
catalysts configuration power density
(mW cm−2)specific capacity
(mAh g−1)open circuit
voltage (V) electrolytes charge/discharge
cycles refs
Fe−Nx−CFe−Nx96.4 641 1.51 6.0 M KOH + 0.2 M
Zn(Ac)2
300 h 126
1.49 hybrid polymer film 120 h
Fe−N4SAs/NPC Fe−N4232 1.5 6.0 M KOH + 0.2 M
ZnCl2
108 (36 h) 144
Fe SAs/N−CFe−N4225 636 1.5 6.0 M KOH 260 h 145
CoNG Co−N4300 785 1.40 6.0 M KOH 15 h
a
146
S,N−Fe/N/CCNT Fe−Nx102.7 1.35 KOH + Zn(Ac)2100 147
Fe-SAs/NPS-HC Fe−N4195 1.45 6.0 M KOH + 0.2 M
Zn(Ac)2
500 (200 000 s) 148
Fe−N/P-C Fe−N3P 133.2 723.6 1.42 6.0 M KOH 40 h 149
pfSAC-Fe Fe−N−C 123.43 732 1.41 8.0 M KOH + 0.5 M
ZnO 300 h 150
Fe SAs/N-G Fe−N4275 738 1.24 120 h 151
Co-POC Co−Nx-C 78 1.5 6.0 M KOH + 0.2 M
ZnCl2
237 (79 h) 152
NGM-Co Co−Nx-C 152 750 1.3 0.2 M ZnCl2+ 6.0 M
KOH 60 h 153
29 1.439 PVA 18
CoSA@NCF/CNF Co−N4530.17 1.41 PVA 90 154
A-Co@CMK-3-D Co−C 162 765 1.25 6.0 M KOH 45 h 155
Co−N3C1@GC Co−N3C1255 1.40 10 h 156
NC-Co SA Co−Nx20.9 mW cm−31.411 Solid-state electrolyte 125 (2500 min) 157
Co-SAs@NC Co−N 105.3 897.1 1.46 6.0 M KOH + 0.2 M
ZnCl2
158
1.40 KOH-PVA 1000 min
CoN4/NG Co−N4115 730 1.51 6.0 M KOH + 0.2 M
ZnO 100 h 159
28 KOH + Zn(COOH)2+
PVA 5h
Cu ISAS/NC Cu−N3280 736 1.43 6.0 M KOH 45 h
a
160
CuSA@HNCNxCu−N3212 806 1.51 6.0 M KOH + 0.2 M
Zn(Ac)2
1800 (300 h) 161
202 793 1.51 biocellulose membrane 1500 (250 h)
Mo SACs/N-C Mo1N1C278 750 1.47 6.0 M KOH + 0.1 M
Zn(Ac)2
360 (120 h) 162
FeCo-IA/NC Fe−N4and
Co−N4
115.6 635.3 1.472 6.0 M KOH + 0.2 M
ZnCl2
100 164
FeCo(a)-ACM Fe−N4159.92 775.91 1.39 6.0 M KOH + 0.2 M
ZnCl2
5400 (900 h) 166
Co−Co3O4@NAC 164 721 1.449 6.0 M KOH + 0.2 M
Zn(Ac)2
195 h 167
SA-PtCoF Pt−Co 125 808 1.28 6.0 M KOH + 0.2 M
Zn(Ac)2
240 h 168
Co SANC-850 Co−N4860.95 1.48 6.0 M KOH + 0.2 M
Zn(Ac)2
44 h 169
a
Stability test at constant discharge current.
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multisite synergy, support design, as well as increasing metal
loading are effective.
SACs in Al-Air Batteries. At the gas−solid−liquid three-
phase interface, only the metal atoms exposed on catalyst
surface can serve as the adsorption/desorption sites for
reaction intermediates. As known, reducing catalyst dimen-
sions to achieve more exposed active sites and promote mass
transfer is a feasible strategy to enhance ORR activity as well as
battery performance. Li et al.
169
synthesized Co−N4active
centers on biomass-derived 3D ultrathin porous carbon (Co
SANC-850) with high specific surface area and rich pore
volume, which could accommodate more active sites and boost
mass transfer. In 0.1 M KOH, the catalysts attached the
relatively positive Eonset (0.995 V), E1/2 (0.863 V) and low
Tafel slope (68.3 mV dec−1), which suggested the great ORR
property and fast kinetic process. The DFT calculations
displayed the smaller energy barriers on Co−N4sites than
those on graphitic N and pyridinic N models. The Al-air
batteries possessed an OCV of 1.8 V and a peak power density
of 494 mW cm−2(Figure 11a). And the voltage did not decay
obviously after constant current density discharge for 10 h,
which demonstrated the great stability (Figure 11b). Similarly,
3D carbon aerogels containing abundant Fe−N4sites
(NCALR/Fe) were prepared for Al-air batteries.
170
SACs in Li-Air Batteries. During the discharge process of
Li-air batteries, the Li2OorLi
2O2continuously accumulated in
air electrode. The catalysts for promoting the formation/
decomposition of discharge products is pivotal.
171
Qian and
co-workers
172
used Pt SAs on ultrathin g-C3N4nanosheets (Pt-
CNHS) as cathode catalysts. Through Pt−CorPt−N bonds
(Figure 11c), the electrons transferred from Pt atoms to g-
C3N4nanosheets. The Pt-CNHS-based Li-air batteries showed
the initial discharge capacity of 17059.5 mAh g−1at the current
density of 100 mA g−1. Also, Xu and co-workers
173
utilized a
combined polymer encapsulation/template replication strategy
to stabilize CoN4moiety on N-doped carbon sphere. The
assembled Li-air batteries displayed a high discharge capacity
of 14777 mA h g−1at 100 mA g−1and higher current densities
under various discharge voltages than Pt/C-based counterparts
(Figure 11d). During the discharge process, CoN4served as
active seeds to form Li2O2nanoparticles and then promoted
the growth of Li2O2nanosheets. The LiO2species were easier
to detach from the N-HP-Co SAC surface and diffuse into the
electrolytes during the charge process (Figure 11e). Therefore,
Figure 11. SACs in Al-air, Li-air and Li-CO2batteries. (a) Discharge polarization and power density plots. (b) Long-time discharge curves of
Al-air batteries. Reprinted with permission from ref 169. Copyright 2020 The Royal Society of Chemistry. (c) FT-EXAFS results. Reprinted
with permission from ref 172. Copyright 2020 Elsevier. (d) Full range rate performances, (e) charge mechanisms and (f) voltage versus cycle
number of Li-air batteries. Reprinted with permission under a Creative Commons CC BY License from ref 173. Copyright 2020 Nature
Publishing Group. (g) Full discharge/charge profiles of Li-CO2batteries. Reprinted with permission from ref 174. Copyright 2020 Wiley-
VC.
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the N-HP-Co SAC promoted the decomposition of Li2O2
through a one-electron process to accelerate the ORR/OER
kinetics. The N-HP-Co SAC electrode endured 261 discharge/
charge cycles at 100 mA g−1and the monodispersed CoN4
configurations were maintained (Figure 11f). This work reveals
the promotion of SACs in the formation/decomposition of
Li2O2, which was instructive for the clarification of reaction
paths and the design of electrode materials.
SACs in Li-CO2Batteries. Similar to Li-air batteries, the
accumulation of solid discharge products also hinders the
progress of Li-CO2batteries. To accelerate the formation and
decomposition of Li2CO3, Dai and co-workers
174
prepared Fe
SAs (Fe−N4) on N, S-doped graphene (Fe-ISA/N, S-HG). In
Li-CO2coin cells, the discharge capacity of 23174 mAh g−1
and charge capacity of 21520 mAh g−1were achieved at the
current density of 100 mA g−1(Figure 11g). At 1.0 A g−1, the
batteries could withstand discharge/charge cycles over 100
times. The addition of N and S caused the charge and spin
redistribution, which accompanied with the formation of Fe−
N4configuration to boost CO2reduction and evolution. DFT
calculations indicated that the Fe−N4moieties displayed a
large output potential, which was consistent with experimental
data. The robust cycle stability and excellent catalytic
performance of catalysts provided a guarantee for improving
the application potential of metal-CO2batteries. To conclude,
the decomposition of discharge products in Li-CO2batteries
should be given great attention. The SACs provide more
opportunities toward the accelerated battery reactions.
Table 3. Summary of SAC-Based Metal-Sulfur Batteries
a
catalysts configuration initial capacity
(mAh g−1)at(x) rate capacity (mAh g−1) after (n)
cycles at (x) rate electrolyte maximum loading
(mg cm−2) refs
Fe-PNC Fe(II)N41138.6 (0.1) 427.1 (300) (0.1) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 1 wt % LiNO3
S 1.3 185
557.4 (300) (0.5)
NC:SAFe Fe−N 1052 (1) 989 (0.5); 589 (12) 1 M LiTFSI in DME/DOL + 1 wt %
LiNO3
Li2S 2.0∼2.3 186
790 (200) (1)
490 (1000) (2)
(3350 mA g−1)
315 (1000) (5)
(8375 mA g−1)
Co−N−CCo−N−C 1247 (0.2) 1035 (2) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 2 wt % LiNO3
S 11.3 187
1161 (0.5) 850 (300) (0.5)
Co@C3N4∼1400 @ 1.6 mA cm−2∼800 @ 12.8 mA cm−21 M LiTFSI and 0.5 M LiNO3in
DOL/DME (1:1, v:v) S 4.0 188
∼980 (200) (1)
(3.2 mA cm−2)
Fe1/NG Fe−N complex ∼1200 (0.2) 891.6 (750) (0.5) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 0.1 M LiNO3
S 4.5 189
∼673 (5)
Ni@NG Ni−N41598 (0.1) 612 (10); 826.2 (500) (1) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 1 wt % LiNO3
S 6.0 190
428.4 (500) (10)
pouch cell
965.8 (200) (1)
Co-N/G Co−N4−C 1210 (0.2) 618 (4) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 2 wt % LiNO3
S 6.0 92
5.1 mAh cm−2
(100) (0.2)
681 (500) (1)
2D MOF-
Co Co−O41138 (0.1) 703 (200) (0.5) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 1 wt % LiNO3
S 7.8 191
∼450 (600) (1)
NC@SA-
Co Co−Nx1160 (0.1) 582 (5) 1 M LiTFSI in DOL/DME (1:1, v:v)
+ 1 wt % LiNO3
S56wt% 192
∼450 (700) (2) 7.2
CoPcCl Co−N41256.3 (0.1) 785 (2) 1 M LiTFSI in DOL/DME (1:2, v:v)
+ 0.1 M LiNO3
S 1.16 195
1124.1 (0.3) 830.9 (200) (0.1)
SAV@NG V−N41230 (0.2) 770 (100) (0.2) 1 M LiCF3SO3in DOL/DME (1:1,
v:v) + 0.1 M LiNO3
S5 196
780 (0.5) ∼551 (400) (0.5)
Co-HC single atomic Co and
Co clusters 1081 @ 100 mA g−1508 @ 100 mA g−1(600) 1 M NaClO4in PC:EC (1:1, v:v) + 5
wt % FEC S47wt% 193
220.3 @ 5 A g−15.0
Ni−O5Ni−O51040.9 @ 50 mA g−1608 @ 100 mA g−10.8 M KPF6in EC: PC (1:1, v:v) S 35 wt % 194
330.6 @ 1 A g−1(500) 1.2
a
1 C = 1675 mA h g−1based on S weight.
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SACs in Li-S Batteries. As we discussed in the previous
section, the major problem in Li-S chemistry should be the
unmanageable dissolution of polysulfide intermediates and
their further back-and-forth diffusion (so-called shuttle effect).
Hence, encapsulating sulfur in a rational cathode host and
speeding up the redox kinetics of the polysulfide intermediates
appear to be vital. In 2014, inherently polar Ti4O7with the
Magneli phase was reported by the Nazar group, and this
metallic oxide can effectively modify interface-mediated redox
chemistry to trigger the conversion of polysulfides.
175
Inspired
by this work, various catalysts like metal nanoparticles (Pt, Co,
Pd),
176−179
metal nitrides,
180,181
metal oxides,
182
and metal
sulfides
183,184
have been employed in Li-S batteries to boost
the conversion kinetics among both soluble polysulfides and
solid sulfides, which indeed prolonged cycling lifespan and
improved sulfur utilization. Recently, SACs show advantages as
the incomparable atom utilization efficiency (up to 100%). In
addition, since SACs are monodispersed in solid substrates,
and take up less volume and weight in a sulfur cathode,
employment of them is favorable to high-energy lithium-sulfur
batteries. Therefore, the selection of suitable SACs may
catalyze the liquid-to-solid and solid-to-solid reactions by
reducing the energy barrier, restrain the polysulfide shuttle
effects, and guide the lithium deposition in Li-S batteries.
Recently, many reported works have successfully synthesized
various SACs to apply in Li-S batteries, demonstrating
excellent performances for polysulfides conversion (see Table
3). For example, via a combination of a simple nanocasting
method and hard template method, a single Fe atom catalyst
homogeneously dispersed in porous nitrogen-doped carbon
Figure 12. SACs in sulfur cathodes for Li-S batteries. (a) UV−vis absorption spectra of the polysulfide solution. (c) Tafel polarization curves.
(e) Thermogravimetric curves. CV diagrams of the symmetric cells based on (b) Fe-PNC, (d) Co−N−C, and (f) Co−N/G electrodes and
corresponding reference samples. (g) Charge curves with different overpotentials. (h) Calculations of free energy for sulfur species in
reduction stage. Reprinted with permission from ref 185. Copyright 2018 American Chemical Society. Reprinted with permission from ref
187. Copyright 2019 Wiley-VCH. Reprinted with permission from ref 92. Copyright 2019 American Chemical Society.
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matrix (Fe-PNC) was prepared for Li-S batteries.
185
The
produced Fe-PNC showed stronger interaction to trap Li2S6
according to the results based on UV−vis spectra (Figure 12a).
Furthermore, cyclic voltammetry (CV) measurements in
Figure 12b based on symmetric cells with Li2S6electrolyte
clearly revealed the catalytic effect of diversified catalysts on
the redox conversion of polysulfides. As a result, Fe-PNC/S
composites during electrochemical cycles presented higher
specific capacity (1138.6 mAh g−1at 0.1 C), smaller
polarization, and higher rate performance than those of
benchmark cells. Post-mortem analysis of the discharge
product showed well-retained Li2S nanospheres in the Fe-
PNC/S cathode. All these results indicated the kinetic
acceleration in the polysulfide conversion process by Fe-
SACs, which improved the reversible performance and
weakened the shuttle effect. In addition, Fe-SACs have
successfully reduced the decomposition energy barrier of
Li2S and improved the reaction kinetics in the Li2S delithiation
reaction. As a result, the produced Li2S@NC:SAFe nano-
composites demonstrated a discharge capacity of 589 mAh g−1
at an ultrahigh rate of 12 C as well as a long-term cycling
lifespan at 5 C over 1000 cycles.
186
In addition, Li et al.
187
developed a Co−N−C nano-
composite in which adequate atomic-scale Co active sites
coupled with porphyrin as framework conductive substrates to
facilitate stepwise redox reaction of sulfur species. Especially,
the current density of cells using Co−N−C electrocatalyst
consistently outperformed the control one, which means the
high efficiency of the Co−N−C electrocatalyst in chain-
breaking reaction of polysulfides and powerful activation of
initial Li2S. The deeply improved reaction kinetics can also be
obtained from Tafel plots in Figure 12c. According to CV
measurements (Figure 12d), Co−N−C catalyzed the con-
version reactions among polysulfides showing sharper redox
peaks with higher currents. The long-term cycle with 0.1%
cyclic decay was achieved at 0.5 C, from an initial 1161 mAh
g−1to a maintained capacity of 850 mAh g−1. Besides Co−N−
C, single Co atoms dispersed in hierarchical carbon nitride
(C3N4) have been reported for lithium-polysulfide (Li-PS)
batteries.
188
Du and co-workers
92
proposed another cobalt-
based catalyst (Co−N/G) with atomic Co singly dispersed in a
Figure 13. SACs in separators for Li-S batteries. (a) Schematic illustration of the functional separator. (b) Voltammetry curves of Li-S cells at
a scanning rate of 0.1 mV s−1. Reprinted with permission from ref 189. Copyright 2019 American Chemical Society. (c) UV−vis absorption
spectra of Li2S6solution and corresponding digital photographs (inset). (d) Voltammetry curves of symmetric cells. (e) Proposed
mechanism of Ni@NG catalyst. Reprinted with permission from ref 190. Copyright 2019 Wiley-VCH.
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nitrogen-doped graphene matrix. This single-atom catalyst
efficiently promoted the phase transformation among poly-
sulfides to increase S utilization for Li−S batteries. The mass
ratio of sulfur in the S@Co−N/G composite can achieve a
high value of about 90 wt % in a thermogravimetric experiment
(Figure 12e). The symmetric cell with the Co−N/G electrode
demonstrated a maximum current density and relatively lower
voltage hysteresis during the multistep redox process, as shown
by CV curves (Figure 12f). The best electrochemical kinetics
was apparently ascribed to the Co−N/G that effectively
catalyzed polysulfide conversion. The concentration variation
curves of intermediate polysulfides and final Li2S species
during cycling also suggested the improved kinetics in a
complete phase evolution from polysulfides to Li2S. And the
lowest overpotentials in the charge curves for S@Co−N/G
further proved the decreased energy barriers for Li2S
decomposition (Figure 12g). The corresponding theoretical
studies proved the lower Gibbs free energy for Co−N/G in the
whole discharge process, especially in the rate-limiting step of
Li2S2/Li2Sconversion(Figure 12h). In the subsequent
electrochemical studies, the S@Co-N/G cathode could deliver
a capacity of 1210 mAh g−1at 0.2 C with sulfur loading of 2.0
mg cm−2and improved rate capabilities. Surprisingly, with an
ultrahigh mass ratio (90 wt %) and practical S loading of 6.0
mg cm−2, the S@Co−N/G cathode still showed superior
performance with a 0.029% decay rate after 100 cycles. This
Figure 14. SACs in separators/interlayers for Li-S batteries. (a) Schematic illustration of the assembled Li-S pouch cell with a B/2D MOF-
Co separator. (b) Comparison of Li2S6adsorption capacity with different materials. Reprinted with permission from ref 191. Copyright 2020
Wiley-VCH. (c) Working mechanism of multifunctional interlayer in Li-S batteries. (d) Catalytic action of NC@SA-Co for polysulfides
conversion. (e) CV diagrams of the symmetric cells. Reprinted with permission from ref 192. Copyright 2020 Wiley-VCH.
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work has significant implications for devising advanced sulfur-
based cathode with single atom catalysts, as well as provides an
approach to realize high-performance Li-S batteries under
more practical conditions for further industrialization.
Author: Please verify that the changes made to improve the
English still retain your original meaning.Recently, SACs have
been employed to construct functional separators or interlayers
for Li-S batteries. Zhang et al.
189
proposed the multifunctional
separator with the coating of N-doped graphene foam (NG) in
which single-atom catalysts such as Fe, Co, or Ni atom were
fully impregnated (Figure 13a). The sample with Fe1/NG
showed the strongest bonding to polysulfides. As a multifunc-
tional separator, the additional catalytic action of SACs was
demonstrated in further electrochemical measurements. Cyclic
voltammetry exhibited the improvements of polysulfides redox
chemistry for Fe1/NG-modified separators, such as the obvious
reduction of the voltage gap and higher current response
(Figure 13b). After long-term cycling over 750 cycles, the Li-S
batteries still delivered superior discharge capacity with 891.6
mAh g−1at 0.5 C. Moreover, the modified separator resulted in
good rate capabilities from 0.2 to 5 C while it delivered a
discharge capacity of 673 mAh g−1at 5 C. Zhang et al.
190
fabricated a modified separator coated by Ni@NG composite
that are single Ni atoms distributed in nitrogen doped
graphene (NG). The restraint to polysulfide shuttling by
Ni@NG was intuitively presented in Li2S6adsorption experi-
ments and UV-vis spectra, resulting in the lightest color in
Figure 13c. Two pairs of obvious redox peaks and high
response current in CV curves also proved the improved
kinetics in polysulfides conversion process (Figure 13d). The
calculated exchange current density derived from Tafel plots
also verified the enhanced catalytic activity in Li-S batteries.
Figure 15. SACs for Na-S and K-S batteries. (a) Schematic illustration of S@Con-HC. Schematic illustration of the reaction mechanism in (b)
S@Con-HC and (c) S@HC cathodes. (d) Long cycle performance RT-Na/S batteries. Reprinted with permission under a Creative Commons
CC BY License from ref 193. Copyright 2018 Nature Publishing Group. (e) Calculations of free energy of potassium sulfides during
reduction. (f) Cycling performance for potassium storage at 1000 mA g−1. (g) Schematic illustration of synthesis process of the NiSA/S/C
nanotubes. Reprinted with permission from ref 194. Copyright 2020 Wiley-VCH.
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Good rate performance confirmed the kinetic conversion of
polysulfides was visibly improved as well, delivering a satisfying
capacity of 612 mAh g−1at 10 C. Further DFT calculation was
adopted to clarify the working mechanism of Ni@NG,
revealing the great reduction of the Li2S decomposition energy
barrier from 1.98 to 1.23 eV. Therefore, the kinetics during the
delithiation reaction of Li2S was more favorable with the
presence of single Ni atoms on NG. The catalytic mechanism
was clearly identified with XPS spectra, Ni K edge XANES
spectra, and Raman spectra, as shown in Figure 13e. The peak
in XPS assigned to the bonding between Sx2−and Ni−N could
be used as an explanation that this strong interaction can
efficiently capture polysulfide from their dissolution as well as
catalyze the conversion process. Moreover, the low decom-
position energy barrier of Li2S and reduced free energy of
conversion reaction among LiPS would facilitate the reversible
electrochemical process even more to render excellent
performance. This work illustrates the significant sights and
feasible applications of single Ni atoms incorporation with the
separator in Li-S batteries.
Moreover, the research findings by Li and co-workers
191
reported that a single Co atom array mimic could ensure safe
and long life Li-S batteries. They prepared a bifunctional
separator (B/2D MOF-Co), combining with bacterial cellulose
(BC) and two-dimensional ultrathin metal organic framework
nanosheets with loading of Co atoms. Introducing this
separator into the Li-S system would not only induce uniform
Li plating with strong interaction between Li and surface O
atoms to eliminate the dendrite growth, but also effectively
restrain the shuttle effect via Lewis acid−base interaction to
trap soluble polysulfides. Beyond coin cells, the practicability of
this separator was further investigated with a flexible pouch cell
(Figure 14a) at different bending angles. Furthermore, the
Li2S6captured by 2D MOF-Co was determined by UV−vis
spectra, showing its stronger adsorption over other reported
materials (Figure 14b). Thus, Li-S cells based on the
bifunctional separator with single Co atoms showed safe and
stable cycling performance. Interlayers, as an additional
component in Li-S cells shown in Figure 14c, can play a
very valid role in governing the transport behavior of
polysulfides. Hence, finding an ideal interlayer would
effectively push forward the practical applications of Li-S
batteries. For example, a multifunctional interlayer (denoted as
C−C−N−Co) containing single-atom cobalt was successfully
developed and applied in Li-S batteries by Guo and co-
workers.
192
An abundant Co−N4structure was revealed by
various microstructures and spectroscopic characterizations
and served as an active site to enhance the redox conversion of
polysulfides during electrochemical cycling (Figure 14d). With
the CV test of symmetric cells, the C−C−N−Co electrodes
showed the highest peak current and smallest overpotential,
demonstrating the ability to accelerate the conversion reaction
(Figure 14e). Therefore, the Li-S battery with this interlayer
can exhibit improved rate performance and long cycle life
(more than 700 cycles at 2 C).
Overall, those works have demonstrated the powerful roles
of various SACs in tackling series of challenges in Li-S
batteries, including the efficient restrictions on dissolved
polysulfides and obvious enhancement for their corresponding
redox conversion within the cathode matrix or modified
separators. Thus, with the minimization of the shuttle effect
and the maximization of the polysulfides redox kinetics, the
overall performances of high-energy Li-S batteries have
improved significantly. However, considering that the work-
place for SACs functioning in cathodes and functional
separators mainly locates at the host/matrix surface, decent
host/matrix structures with appropriate loading of active SACs
should be further designed and developed. Additionally, more
atomic-level mechanistic insights via advanced experimental
characterization techniques and theoretical calculation are
quite advisable to guide the efficient design of SACs.
SACs in Na-S Batteries. As for Na-S@RT batteries, the
relevant exploration and application of SACs in this field are
still comparatively rare (see Table 3). Correlative research was
carried out by Zhang et al.,
193
where they used hollow carbon
(HC) nanospheres as the sulfur host with atomic Co
embedded in a carbon shell. This configuration of a composite
cathode noted as S@Con-HC (Figure 15a) maximized the
electrocatalytic activity of atomic Co, effectively improving the
overall performance of Na-S@RT batteries. According to their
studies, the dispersion of Co species including both Co clusters
and single atomic Co in C shells were revealed by HADDF-
STEM and XPS results. The sulfur content in S@Con-HC was
identified at 47 wt %. Then, the catalytic effect of atomic Co
was further evidenced with cyclic voltammograms for S@Con-
HC, showing two obvious cathodic peaks at around 1.68 and
1.04 V during the initial scan. This clear and concise reaction
process demonstrated the fast kinetics of sodiation without
unnecessary peaks of various polysulfides. The deep reaction
mechanism was further revealed by in situ XRD and Raman
spectroscopy. The final reaction product was confirmed as
Na2S, accompanied by the fast transition of Na2S4to Na2S.
DFT calculations were done to further support the proposed
reaction mechanism without and with Co6cluster on carbon
substrate. The stronger adsorption energy of sodium
polysulfides with Co6cluster confirmed the fast conversion
kinetics. Therefore, as shown in Figure 15b and c, the atomic
Co in C shells could restrain the dissolution of polysulfides via
polar−polar attraction. Moreover, multifunctional atomic Co
could catalyze the remaining polysulfides in C shells to rapidly
switch into Na2S. Thus, the shuttle effect was validly relieved
and redox reactions could be more thorough. As a result, the
enhanced cycling stability could be obtained from the S@Con-
HC cathode as shown in Figure 15d, demonstrating a
discharge capacity of 508 mA h g−1at 100 mA g−1after 600
cycles.
SACs in K-S Batteries. Beyond those electrodes for Li/Na
storage, a recent research by Lin and co-workers
194
suggested
that single-atom design could also boost the performance of
potassium storage (K-storage) via enhancing conversion
kinetics in the K−S chemistry (Figure 15g and Table 3).
They developed the Ni/S/C ternary composite nanotubes
comprising the small-molecule sulfurs as active materials for
potassium ion batteries (PIBs). The physical structure of the
active Ni site was further identified by XANES and EXAFS,
showing the clearly isolated Ni−O5structure. Moreover, DFT
calculations corroborated the advantage of the atomically
dispersed Ni in the isolated Ni−O5structure. The Gibbs free
energy of the rate-limiting reaction, that is, the reversible
conversion between K2S2to K2S, was obviously decreased
(Figure 15e). The results indicate the reversibly electro-
chemical kinetics of the potassium sulfate (K2Sx,x≤3) during
charge and discharge was sharply raised. Various electro-
chemical measurements including GITT voltage profiles, Tafel
plots, and CV curves also exhibited the lower overpotential of
the NiSA/S/C nanotube during the potassiation and depot-
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assiation process. In consequence, the NiSA/S/C nanotubes
can deliver an outstanding capacity for high K-storage of 608
mAh g−1(calculation based on the mass of the composite)
under a current of 100 mA g−1(Figure 15f).
With the method of surface sulfurization involving single
metal atoms, both the conductivity and utilization of active
sulfur can be improved. Moreover, exploring more various
metal centers in the optimized coordination environment
might exhibit higher catalytic activity and tighter affinity for
polysulfides. Hence, more stable cycling and higher S
utilization in Li/Na/K-S batteries can reasonably expect to
be realized by suitable SACs. At the same time, attention will
also need to be given to the key challenges on the anode side,
because the uneven SEI layer and the uncontrollable metal
Figure 16. SACs for Li and Na metal anodes. (a) Schematic illustration of the induced dendrite-free morphology. (b) Comparison of Li
nucleation overpotentials. Reprinted with permission from ref 198. Copyright 2019 Wiley-VCH. Schematic illustration of the Li deposition
behavior and corresponding energy distribution mappings of Li adsorption on (c) pristine graphene (PG) and (d) SA metal@nitrogen-
doped graphene (SA metal-NG) anodes. Reprinted with permission from ref 199. Copyright 2019 Wiley-VCH. (e) Scheme of the Li
deposition process. Reprinted with permission from ref 200. Copyright 2019 American Chemical Society. Schematic illustrations of Na
deposition behavior on (f) bare Cu substrate and (g) ZnSA−N−C electrodes. Reprinted with permission from ref 202. Copyright 2019
American Chemical Society.
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dendrite growth would cause premature failure of metal-sulfur
batteries.
SACs in Li/Na Metal Anodes. Li metal batteries have
been viewed as promising candidates for next-generation high-
energy rechargeable batteries.
197
Therefore, high-performance
Li metal anodes are rather important. However, the Li dendrite
issue is always a big hindrance. Some recent works shed
substantial light on the controllable lithium nucleation via
homogeneously distributed single atoms. The representative
work involving single atoms to guide lithium deposits was
demonstrated by Zhang and colleagues.
198
They explored
carbon substrate with atomically Co and N atoms doping
(CoNC) to serve as lithium host. The uniform distribution of
Co was achieved with a Co−N coordination link, while the
local electronic structure was simultaneously tailored to
promote the adsorption and even nucleation of lithium (Figure
16a). Moreover, this hierarchical framework with sufficient
interior spaces could facilitate rapid diffusion of Li ions and
endure the infinite volume changes during the repeated
electroplating/striping cycles (Figure 16b). Accordingly, the
lithium deposition showed smooth morphology, and the
CoNC-Li composite anodes afford superb performances such
as a high CE of 98.2% even at 10.0 mA cm−2. Using a similar
host, nitrogen-doped graphene (NG), Zhai et al.
199
prepared
the composite anodes with the doping of different single-atom
metals (Ni, Pt, Cu). The introduction of metal atoms showed
an effective increase in the Li adsorption energy by DFT
calculations, which contributed to the experimentally uniform
Li deposition. In addition, the formation of a metal−N−C
coordination structure would be beneficial for maintaining the
atomic structural stability (Figure 16c, d). Thus, high-
performance Li anodes without dendrites were achieved,
exhibiting a high CE of 98.45% over 250 cycles and a stable Li
plating/stripping performance at 4.0 mA cm−2. Also, single
iron atoms dispersed in a N-doped carbon matrix could act as
lithiophilic sites and minimize the Li nucleation overpotential
(as low as 0.8 mV) (Figure 16e).
200
Further molecular
dynamics (MD) simulations proved the enhanced affinity
between the atomic Fe−N−C sites and Li ions. This strong
interaction could ensure the stable and uniform Li plating/
stripping behaviors and, more importantly, the obvious
suppression of dendrite growth. When FeSA−N−C/Li matched
with LiCoO2, the full cells showed long-life cycling over 200
cycles. When choosing MXene layers as the substrate, the
presence of single zinc atoms showed the ability of inducing
dendrite-free deposition.
201
DFT simulations revealed the low
energy barrier during Li migration and high surface binding
energy on the Zn single-atom (ZnSA) surface. In addition,
microscopic results validated the homogeneous Li nucleation
near the Zn atoms via forming a bowl-like morphology. As a
result, Li-ZnSAs anodes demonstrated a low overpotential for
Li deposition, long lifespan, and stable cycling performance
under various rates.
Moreover, to address the problems of Na metal anodes, Yan
and co-workers
202
proposed the combination of carbon
substrates and single Zn atoms (namely, ZnSA−N−C) to
achieve the even Na deposition. The homogeneous distribu-
tion of Zn atoms in substrates induced adequate sodium-philic
sites, where the Na electroplating presented good selectivity to
nucleate, refraining from the dendrite formation (Figure 16f,
g). In addition, the strong chemical affinity between ZnSA−N−
C and Na ions proved by DFT calculations and near-zero
nucleation overpotential further elucidated the reduced
nucleation barriers and controlled the nucleation behavior.
Figure 17. Performance of reported SAC-based (a) Zn-air batteries and (b) PEMFCs.
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Consequently, superior Na electroplating/stripping perform-
ances were exhibited such as high CE of 99.8% upon 350
cycles and excellent cycle life over 1000 h in symmetric cells. In
addition, a full-cell configuration with Na3V2(PO4)3and Na−
ZnSA−N−C electrode delivered good cycling stability over
1000 cycles with a CE of 100%. Hence, the SAC-modified
hosts can promote the uniform Li/Na deposition and show the
validity of the protection of metal anodes. Nevertheless, more
related works on safeguarding metal anodes remain to be
further developed, which is not only confined to the even Li/
Na deposition but also the complete suppression of the
polysulfides corrosion onto the active metal.
CONCLUSIONS AND PERSPECTIVES
In summary, we have concluded different cases of SACs
applied in various energy storage (or conversion) devices,
including PEMFCs, metal-gas batteries, metal−sulfur batteries
and metal-ion batteries. When it comes to ORR, M−N−C
sites are currently the promising ORR catalysts to replace the
precious metal Pt. Plenty of experimental data show that the
homogeneously distributed metal SACs display exceeded ORR
performances compared to cluster or nanoparticle counter-
parts. The coordination unsaturated environment provides
suitable adsorption sites of reactant molecules, while the
metal−support interactions regulate the electronic structure of
central metal SAs and enhance their intrinsic activity.
At present, Fe−N−CandCo−N−Carethemost
commonly studied ORR active sites, consistent with the
activity trend predicted by Cheng’s work.
203
Figure 17 shows
the performance level of current SAC-based PEMFCs and Zn-
air batteries. On the whole, the significant differences in power
density of PEMFCs under H2/O2or H2/air conditions are
observed. And the Fe SAC-based Zn-air batteries demonstrate
relatively higher power density than the others. For metal−
sulfur batteries, the introduction of SACs efficiently promotes
the overall performances because of the activated adsorption
and high activity in sulfur conversion. The meaningful works in
the future should focus on how to choose the adaptive SACs
with scientific theoretical guidance. Despite the impressive
achievements that have been made, the pace of progress is not
enough. The future perspectives are put forward as follows:
Diversification of Active Sites. The design of SACs is not
limited to the known Fe−N−C and Co−N−C sites. To
prepare SAs on carbon-based supports, the choice of metal
sources and organic ligands will affect the microscopic
coordination environment. The related explorations could
direct the modification on active sites, which are significant but
scarce. Also, construction of the multiple metal centers, even
the nonmetal centers, as well as the various coordination
elements from different supports (oxides, sulfides, selenides,
etc.) or heteroatom doping are important approaches. The
coexistence of multimetal sites in SACs provides more
opportunities for the bifunctionality of catalysts, such as
ORR/OER for rechargeable Zn-air batteries.
High-Throughput Synthesis and Performance Pre-
diction. The routine experimental process in the laboratory
wastes a lot of chemical resources and consumes valuable time
and effort. Rapid property screening through high-throughput
design and automated operation will undoubtedly enhance
production efficiency and reduce meaningless efforts. Fur-
thermore, theoretical simulation to predict catalytic perform-
ance serves as a powerful tool which improves experiment
efficiency. Such high-throughput synthesis and theoretical
simulation are also critical ways to achieve the large-scale
applications of SACs in energy-related devices.
The Adaptability of SACs in Electrolytes. Changing the
application environment of SACs from alkaline solution to
other medium, including the acidic environment in PEMFCs,
organic electrolyte systems in Li-air batteries, etc., poses
challenges for the applicability and durability of those catalysts.
As supports of M−N−C species, N-doped carbon materials are
susceptible to erosion by acidic or organic environments.
Considering the requirements for battery durability, this
problem must be optimized.
In-Depth Mechanistic Investigation. Due to the micro-
level constraints, to directly and accurately realize an in-depth
mechanism is difficult. Some recent studies indicated that the
reconstruction of SACs under potentials could happen. Hence,
various in situ techniques will provide significant effects to
figure out the true active species and uncover the reaction
process. Theoretical calculations could construct catalytic
models and assess reaction barriers. The alliance between in
situ techniques and theoretical calculations will present the
profound catalytic mechanisms and structure−activity relation-
ships, which is meaningful to guide the material designs.
Design for Metal-Sulfur Batteries. In order to
sufficiently catalyze the polysulfides conversion, abundant
SACs are always required on the surface of the cathode host.
Hence, with ever-increasing sulfur loading in the cathode to
satisfy the practical application, higher loading of durable SACs
in the cathode host is necessarily imminent. Though the sulfur
electrode grows thicker, the mass transportation and phase
transition should be steady. The cell separator is also a wide
application space of SACs. With the bidimensional architecture
for functional separators and their specialized capability to
convert the dissociative polysulfides, the lower amount in using
SACs could be possible and their effects could be achieved to
the utmost degree. Thus, from the future commercialization
perspective, high areal sulfur loading with a suitable amount of
SACs embedded in lightweight substrates is an optimal
direction. While for designing the functional separators toward
practical metal-S batteries, it is better to serve as a highly
efficient barrier and catalytic converter for polysulfides with
lower amounts of SACs. Just as important, the works of SACs
in enhancing metal anodes should be studied, which would be
a promising strategy for future metal-sulfur batteries.
Toward Practical Application. The actual operating
environment brings additional demands toward SAC-based
electrode materials. Reasonable modification of the electrode
interface and regulation of its hydrophilic/hydrophobic
properties are helpful to optimize the adsorption/desorption
at the reaction interface, therefore improving the output
capacity. Since the agglomeration of metal atoms restricts the
activity of SACs, some synthesis strategies are further needed
to keep exploring to maintain the good dispersion of SAs. As
the synthesis technology improves, large-scale production of
SACs with sufficient active sites would strongly spur on the
practical applications of the battery fields.
In conclusion, opportunities and challenges of SACs exist
side by side. Maintaining the activity and stability of metal SAs
while increasing the loading as much as possible is a conflict
that must be solved before practical application. Also, the high
selectivity of SACs displays disadvantages in bifunctional/
multifunctional catalysis, remaining to be resolved. In addition
to the energy systems discussed above, SACs could also be
widely applied in more electrochemical systems.
ACS Nano www.acsnano.org Review
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232
AUTHOR INFORMATION
Corresponding Authors
Feixiang Wu −School of Metallurgy and Environment,
Engineering Research Center of the Ministry of Education for
Advanced Battery Materials, Central South University,
Changsha 410083, P. R. China; orcid.org/0000-0002-
9688-2428; Email: feixiang.wu@csu.edu.cn
Yongpeng Lei −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China;
Email: leiyongpeng@csu.edu.cn,lypkd@163.com
Authors
Yuchao Wang −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China
Fulu Chu −School of Metallurgy and Environment,
Engineering Research Center of the Ministry of Education for
Advanced Battery Materials, Central South University,
Changsha 410083, P. R. China
Jian Zeng −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China
Qijun Wang −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China
Tuoya Naren −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China
Yueyang Li −State Key Laboratory of Powder Metallurgy,
Hunan Provincial Key Laboratory of Chemical Power
Sources, College of Chemistry and Chemical Engineering,
Central South University, Changsha 410083, P. R. China
Yi Cheng −School of Metallurgy and Environment,
Engineering Research Center of the Ministry of Education for
Advanced Battery Materials, Central South University,
Changsha 410083, P. R. China
Complete contact information is available at:
https://pubs.acs.org/10.1021/acsnano.0c08652
Author Contributions
§
Y.W. and F.C. contributed equally.
Notes
The authors declare no competing financial interest.
ACKNOWLEDGMENTS
This work was financially supported by the Innovation-Driven
Project of Central South University (No. 2019CX033), the
National Natural Science Foundation of China (No:
51904344), and the Hunan Provincial Science and Technology
Plan Project (No. 2017TP1001, 2020JJ4710)
VOCABULARY
Voltage hysteresis, voltage difference between the charge and
the discharge flats; multiple-electron transfer reaction, reaction
with more than one electron transfer per redox center; SEI,
ion-conductive solid electrolyte interphase (a layer) formed on
electrode surfaces from decomposition products of electro-
lytes; ALD, atomic layer deposition, a method for plating
materials layer by layer on substrate surface in the form of
single atomic film; GITT, galvanostatic intermittent titration
technique (GITT), widely applied in battery research to study
the diffusion of lithium in electrode materials
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