2 Principle of Water Splitting
Water splitting is one of the important clean energy technologies and is the major
source of hydrogen, the highest gravimetric energy density fuel. This electrochemical
technology is a combination of two half-reactions: HER and OER.[28],[29] Furthermore, it is considered as an environmentally friendly way for large-scale
H2 production in comparison with the existing methods (e.g., steam reforming). In particular,
splitting a water molecule into hydrogen (H2, HER) and oxygen (O2, OER) molecules is a sluggish chemical process, which, in principle, requires a thermodynamic
voltage of 1.23 V (at 25 °C). Moreover, kinetics of these electrochemical reactions
significantly influence the output performance of the energy conversion devices. Specifically,
due to the resistances and the intrinsic activation barriers present on electrodes,
a much higher voltage than the standard thermodynamic voltage is generally required.
This excess potential needed is known as overpotential (η). To minimize this overpotential
and to achieve as high a current density as possible, a powerful electrocatalyst is
thus applied, which is the central issue of the development of prominent water splitting.
On the other hand, there are some indicators that have been set to appraise the electrocatalyst
performance in water splitting, including current density (j), Tafel slope (b), electrocatalyst stability, and Faradaic efficiency. Current density defines the
electrocatalyst activity, which is expressed as either mA · mg−1 (normalized to electrode mass) or mA · cm−2 (normalized to electrode geometric area) under an applied potential. The Tafel slope,
in particular, expresses the catalytic mechanisms for the electrode reactions, which
is obtained from the slope of the Tafel plot (η = b log(j) + a). The stability determines the practical adaptability of an electrocatalyst that
can be examined by both chronoamperometry and chronopotentiometry. Meanwhile, Faradaic
efficiency describes the charge efficiency in which the electrons are utilized to
form hydrogen. The electrocatalyst should be able to optimize those indicators, requirements
that are always under research focuses.
2.1 Hydrogen Evolution Rection
The H2 evolution is a multistep two-electron transfer reaction involving the adsorption
of hydrogen/water, reduction of dihydrogen and desorption of the formed intermediate
either in acidic or alkaline media. These steps can be classified as a Volmer step,
in which the adsorption of hydrogen on the catalyst surface takes place (eq. [1] and [2]) during the reduction of protons. Meanwhile, through either the Heyrovsky step (eq. [3] and [4]) or the Tafel step (eq. [5] and [6]), molecular H2 will be formed by the combination of H* species (the * indicates the active sites
on the catalyst surface and H* is the absorbed hydrogen). Thus, to evolute H2 from the reduction of protons/water on the catalytic sites in an acidic electrolyte,
for example, HER may occur through either the Volmer–Heyrovsky or Volmer–Tafel path.
Meanwhile, in basic solutions, the protons are in the form of water molecule and thus
the discharge species will be H2O to form the H* and H─O bonds by releasing OH− to the electrolyte. In particular, Pt is regarded as benchmark catalyst for unbeatable
electrocatalytic HER and has an extremely high exchange current density and a small
Tafel slope.[30]
Volmer step
* + H+ + e─ → H* (acidic) (eq. 1)
* + H2O + e─ → H* + OH─ (alkaline) (eq. 2)
Heyrovsky step
H+ + e─ + H* → H2 + * (acidic) (eq. 3)
H2O + e─ + H* → H2 + OH─ + * (alkaline) (eq. 4)
Tafel step
2H* → H2 +2* (acidic) (eq. 5)
2H* → H2 +2* (alkaline) (eq. 6)
2.2 Oxygen Evolution Rection
The electrochemical O2 evolution, the other half-reaction in water splitting, is a four-electron transfer
reaction and struggles even more with its kinetically sluggish nature and a high overpotential.
The OER mechanism is sensitive toward structure of the electrode surface, material
types, and involves several intermediate species such as OH*, OOH*, and O* that are
produced during reaction and react to generate O2 (eq. [7] and [8]).[28] This complicated mechanism causes more critical steps that need to be considered
in both acidic and basic solutions, as it involves the breaking of H–O bonds and subsequent
formation of O=O bonds. Despite its high cost and scarcity, RuO2 has been the benchmark catalyst for OER with an overpotential as small as 420 mV
compared to other noble-metal oxides.[31] However, RuO suffers from chemical instability, especially in acidic solutions at
a high anodic potential (> 1.4 V).[32]
Acidic condition: H2O → O2 +4 H+ +4 e─ (eq. 7)
Mechanism:
* + H2O → OH* + H+ + e─
OH* → O* + H+ + e─
2O* → 2* + O2
O* + H2O → OOH* + H+ + e─
OOH* → O2 + H+ + e─
Basic condition: 4 OH─ → 2O2 +2H2O + 4 e─ (eq. 8)
Mechanism:
* + OH─ → OH* + e─
OH* + OH─ → O* + H2O + e─
2O* → 2* + O2
O* + OH─ → OOH* + e─
OOH* + OH─ → O* + O2 + H+ + e─
3 COF-Based Water Splitting Electrocatalysts
3.1 Potential COFs as Water Splitting Electrocatalysts
As an emerging crystalline porous polymer, COFs have found great applications in electrocatalysis.
In particular, for a decent electrocatalyst, it should show favorable catalytic activity,
desired selectivity, and yet good durability. In this regard, with controllable synthesis
and predictable properties,[24] COFs are expected to fulfill these criteria. COFs are constructed from predesigned
building units with a variety of chemical compositions and electroactive functionals
to create rigid and electroactive porous polymers.[22] Moreover, several COFs exhibited some intriguing characteristics, such as high specific
surface areas (up to 4210 m2 · g−1), tunable pore sizes (up to 4.7 nm), exceptional thermal (up to 600 °C) and chemical
stabilities, and high charge mobility (up to 8.1 cm2 · V−1 · s−1).[19],[33],[34] As a result, COFs provide fully exposed and accessible catalytic active sites which
are crucial to improve the efficiency, selectivity, and to reduce reaction energy
barrier. Furthermore, the presence of nano-to-mesoporous channels serves as effective
electron-transfer and mass-transport pathways and also enables the effective confinement
of single atoms, nanoparticles, and nanocluster electrocatalysts. In addition, the
π-conjugated structures in most of COFs contribute to the electronic conductivity,
which can facilely be improved by heteroatom incorporation, dopant control, and chemical
environment manipulation.[16] More importantly, the reticular synthesis of COFs provides insight into the structure–activity
relationship, which is pivotal to provide understanding of the electrocatalytic mechanism
and modulation. All these critical properties lead to promising application as water
splitting electrocatalysts.
3.2 COF-Based HER electrocatalysts
Although COFs in general possess low intrinsic conductivity and moderate stability
under electrocatalytic conditions, a number of 2D/3D COFs haven been explored as great
alternative HER electrocatalysts ([Table 1]). The first effort in exploring COFs as an HER electrocatalyst was reported by Pradhan
and co-workers in 2017.[35] The team synthesized an electroactive quasi-2D COF (SB-PORPy) via a Schiff-base
condensation reaction of a porphyrin (5,10,15,20-tetrakis-(4-aminophenyl)porphyrin,
TAP) with a pyrene (1,3,6,8-tetrakis(4-formyl-phenyl)pyrene, TFFPy) building unit
to afford a square-like pore COF ([Figure 1a]). SB-PORPy exhibited a high Brunauer–Emmett–Teller (BET) surface area of 869 m2 · g−1 with an accessible pore width of 1.8 nm ([Figure 1b]). The idea of stitching porphyrin and pyrene units could give rise to a conducting
channel derived from the π electronic conjugation of the AA layer stacking mode. Furthermore,
the N-imine (-C=N-) species in the SB-PORPy were considered as perfect free-docking
sites for HER upon protonation, forming positive hyperporphyrinic sites. Accordingly,
SB-PORPy was employed as an electrocatalyst for HER by mechanically grinding it (2 mg)
with carbon-black (1 : 1 weigh ratio) in 0.5 M H2SO4 aqueous solution. Remarkably, the SB-PORPy-based electrode exhibited high current
density and an overpotential of 380 mV at 5 mA · cm−2 for HER, much lower than other reported metal-free COFs, as well as Vulcan and bare
glassy carbon electrodes ([Figure 1c]). Although additional carbon-black is required to improve conductivity, the results
of this work thus imply the potential use of metal-free COFs as HER electrocatalysts.
Furthermore, the Tafel slope obtained from the polarization curve was about 116 mV · dec−1, indicating that the hydrogen evolution mechanism followed the Volmer–Heyrovsky pathway
in which the H–H combination was driven by the help of other adjacent imine nitrogen
sites to evolute hydrogen from the surface ([Figure 1d]). More importantly, the electrode shows decent electrocatalytic stability even after
500 cycles with negligible change in terms of both onset potential and current density
at a scan rate of 100 mV · s−1. This work, as the first case, inspires that metal-free HER electrocatalysts can
be designed by simply reticulating an electroactive component into COFs. More advanced
achievement was reported by Li and co-workers in 2019, in which the team developed
a free-standing 2D conjugated (C–C linked) COF film (2DCCOF1) as a metal-free COF
HER electrocatalyst.[37] The 2DCCOF1 film was prepared by Suzuki coupling polymerization on a water–toluene
interface in 1,4-bis(4,4,5,5-tetramethyl-1,3,2-dioxaborolan-2-yl)benzene with 1,3,5-triiodobenzene
to afford a C–C linked 2DCCOF1 film in the presence of Pd(PPh3)4 as a catalyst. The resultant thin film possessed millimeter lateral size and its
crystalline domain can be visualized under high-resolution transmission electron microscopy.
Structurally, 2DCCOF1 was a layered graphene analogue with homogeneous pore[53], making it a potential material for energy storage and optoelectronic applications.
Subsequently, 2DCCOF1 was deposited horizontally on the copper electrode. Notably,
the 2DCCOF1 film exhibits excellent HER activity compared with that of bare copper
electrode with an overpotential of 541 mV (at 10 mA · cm−2) and a Tafel slope of 130 mV · dec−1. Hence, it is assumed that HER active sites arise from the good electronic conductivity
and the well-arranged graphitic-like structure of the 2DCCOF1 film.
Table 1 Tabulated COF-based water splitting electrocatalysts
COF-based electrocatalysts
|
Electrocatalytic system
|
Surface areasa/pore size (m2 · g−1/nm)
|
Electrode active mass (mg · cm−2)
|
η
(mV, at 10 mA · cm−2)
|
b
(mV · dec−1)
|
Ref.
|
Note: aBased on the Brunauer–Emmett–Teller (BET) method. bMeasured at a current density of 5 mA · cm− 2. cMeasured at a current density of 1 mA · cm− 2. dElectrode active mass indicated as μg; – = data are unavailable.
|
Metal-free COFs
|
SB-PORpy
|
HER
|
869/1.8
|
–
|
380b
|
116
|
[35]
|
PY-SE-COF
|
HER
|
998.03/2.64
|
–
|
–
|
263
|
[36]
|
2DCCOF1 film
|
HER
|
–/–
|
–
|
541
|
130
|
[37]
|
BPT-COF-rGO
|
HER
|
–/–
|
–
|
45
|
53
|
[40]
|
H2PcCOF
|
OER
|
467/1.2
|
3
|
> 430
|
121
|
[45]
|
IISERP-COF3
|
OER
|
2022/2.5
|
5d
|
400
|
–
|
[49]
|
Tp-Tta COF
|
OER
|
716/1
|
1
|
430
|
129
|
[50]
|
C4-SHz COF
|
OER
|
1224/1.85
|
0.07
|
320
|
39
|
[51]
|
JUC-630
|
OER
|
907/2.35
|
–
|
400
|
104
|
[52]
|
Metal-containing COFs
|
CoTcPP
|
HER
|
441.74/–
|
0.08
|
475
|
–
|
[29]
|
PY-SE-COF-Pd
|
HER
|
717.73/2.64
|
–
|
128
|
150
|
[36]
|
Ru@COF-1
|
HER
|
912/1.7
|
–
|
200
|
140
|
[38]
|
c-CNT@TpBpy-Ru
|
HER
|
–/–
|
0.5
|
112
|
–
|
[39]
|
Co-TpBpy
|
OER
|
450/–
|
–
|
400c
|
59
|
[41]
|
Macro-TpBpy-Co
|
OER
|
387/–
|
0.25
|
380
|
54
|
[42]
|
CoTAPP-PATA-COF
|
OER
|
943.72/1.1
|
0.2
|
420
|
56
|
[43]
|
CoTAPP-BDTA-COF
|
OER
|
1047.82/1.2
|
0.2
|
470
|
57
|
[43]
|
NiTAPP-PATA-COF
|
OER
|
–/–
|
0.2
|
670
|
–
|
[43]
|
FeTAPP-PATA-COF
|
OER
|
–/–
|
0.2
|
550
|
–
|
[43]
|
ZJTU-1@Co
|
OER
|
656.8/0.51
|
4
|
295
|
63
|
[44]
|
H2NiPcCOF
|
OER
|
462/1.3
|
3
|
430
|
68
|
[45]
|
NiPcCOF
|
OER
|
323/1.3
|
3
|
410
|
75
|
[45]
|
H2FePcCOF
|
OER
|
326/1.4
|
3
|
430
|
62
|
[45]
|
H2FeNiPcCOF
|
OER
|
346/1.4
|
3
|
430
|
78
|
[45]
|
Ni0.5 Fe0.5@COF-SO3
|
OER
|
281/1.2
|
–
|
300
|
83
|
[46]
|
COF-TpDb-TZ-Co
|
OER
|
–/–
|
–
|
390
|
82
|
[47]
|
Co
x
Ni
y
-IISERP-COF2
|
OER
|
~161.5/–
|
20d
|
258
|
39.8
|
[48]
|
Ni3N-IISERP-COF3
|
OER
|
~606/~2
|
0.07
|
230
|
79
|
[49]
|
Fe-SAC@COF
|
OER
|
716/1
|
1
|
290
|
40
|
[50]
|
Ni-SAC@COF
|
OER
|
~716/~1
|
1
|
337
|
45
|
[50]
|
Fe-NP/COF
|
OER
|
~716/~1
|
1
|
359
|
51
|
[50]
|
Figure 1 The synthesis and HER electrocatalytic performance of SB-PORPy. (a) Solvothermal
synthesis of SB-PORPy and its representative 3D structural model. (b) The N2 adsorption isotherm and pore size distribution of SB-PORPy. (c) Polarization curves
for the HER on bare GCE (blue), Vulcan (red), and SB-PORPy-COF (black) electrodes.
(d) Tafel plot of the SB-PORPy-COF electrode. Adapted with permission from Ref. [35]. Copyright 2017 American Chemical Society.
Although metal-free HER electrocatalysts are low cost and attractive, their performances
are still insufficient. To this end, incorporation of electroactive metals into COFs
has also been performed to improve the electrocatalytic performance of the pristine
COFs or act as HER active sites. In particular, as for earth-abundant elements and
good electroactivity, transition metals are highly potential electrocatalysts.[54] Villagrán and co-workers in 2018 synthesized cobalt porphyrin-based crystalline
polymeric materials for electrocatalytic HER.[29] The polymer was prepared by polymerization of a metalloporphyrin-based CoTcPP (TcPP:
meso-tetra(4-carboxyphenyl)porphyrin) and exhibited crystalline feature as confirmed
by powder X-ray diffraction (PXRD) analysis and showed a moderate specific surface
area of 441.74 m2 · g−1. As metalloporphyrin shows improved activity in biological systems and chemical catalysis,[55],[56] this inspires other authors to employ CoTcPP as an HER electrocatalyst in acidic
0.5 M H2SO4 aqueous solution. As predicted, an electrode composed of CoTcPP (mass loading of
0.08 mg · cm−2) showed HER activity with an overpotential of 475 mV (deposited on FTO glass slides),
which was smaller than that of its discrete CoTcPP molecule (666 mV) at 10 mA · cm−2 cathodic current density. This electrocatalytic activity may arise from the existence
of a porous channel to access the metalloporphyrin active sites. The results identify
that stitching an electroactive component into a repetitive structure improved the
catalytic activity. On the other hand, inspired by remarkable chemical stability of
vinylene-linked COFs,[57] this type of COFs is highly interesting as a host for immobilization of metal-based
electrocatalysts. In this regard, Pd(II) has been deposited on the pore wall of vinylene-linked
PY-SE-COF as a non-platinum electrocatalyst for HER.[36] The PY-SE-COF was prepared through Knoevenagel condensation of 1,3,6,8-tetrakis(4-formylphenyl)pyrene
(TFPPY) with 4,4′-(benzoselenadiazole-4,7-diyl) diacetonitrile (SEA), affording a
high crystalline square-like 2.64 nm mesoporous 2D COF with surface areas reaching
998.03 m2 · g−1. The presence of abundant coordinating sites of N and Se in selenodiazole modules
render PY-SE-COF as a perfect host to accommodate Pd (II) ions. The loading of Pd
into the COF (PY-SE-COF-Pd) can reach 16.8 wt% with minimum reduction of surface areas
(717.73 m2 · g−1) and negligible change of pore size. Notably, PY-SE-COF-Pd exhibited a small overpotential
of 128 mV at a current density of 10 mA · cm−2 when employed as a HER electrocatalyst in an acidic electrolyte (0.5 M H2SO4), outstanding in comparison with the performance of individual PY-SE-COF and PdCl2 (240 mV). Furthermore, PY-SE-COF-Pd exhibited a Tafel slop of 150 mV · dec−1, much smaller than those of individual PY-SE-COF (263 mV · dec−1) and PdCl2 electrodes (245 mV · dec−1). These results clearly identify that the improved HER activity arises from the collective
electrocatalytic capability of each component. More intriguingly, the high chemical
stability of the host leads to the only slight decrease current density even after
2000 CV cycles.
Pristine COFs and transition metal-incorporated COFs offer low-cost HER. However,
their performances are still lower than those of noble-metal electrocatalysts. To
this end, immobilization of noble metals into COFs has been an attractive avenue for
construction of powerful HER electrocatalysts, yet improved catalyst stability toward
corrosion under acidic conditions. Chen and team took advantage of the excellent chemical
stability of vinylene-linked COFs and the good electrical conductivity of triazine-containing
COFs when protonated as a perfect host to immobilize a Ru noble metal catalyst ([Figure 2]).[38] The vinylene-linked COF-1 was prepared by reacting 2,4,6-trimethyl-1,3,5-triazine
(TMTA) with 1,4-diformylbenzene (DFB) in the presence of KOH as a catalyst ([Figure 2a]). The resultant 2D COF-1 was highly crystalline with a high specific surface area
of 1140 m2 · g−1 and established a pore channel of 1.84 nm, making it attractive for noble metal immobilization
([Figure 2b]). Intercalation of Ru metal (7.5 wt%) at room temperature afforded a Ru@COF-1 composite
with minimum reduction of both surface areas and pore size (down to 912 m2 · g−1 and 1.7 nm, respectively). The presence of Ru (III) ion and the significantly retained
porosity and crystallinity render the Ru@COF-1 composite promising as a HER electrocatalyst,
facilitating full contact between reactants and catalytic sites. As a result, the
Ru@COF-1 electrode afforded a small overpotential of 200 mV at 10 mA · cm−1 in an acidic electrolyte (0.5 M H2SO4), smaller than that of RuCl3, while COF-1 was inactive for HER electrocatalysis ([Figure 2c]). This result justifies that the Ru (III) ion was the main HER active site and COF-1
improves the performance by confinement. Furthermore, Ru@COF-1 exhibited a Tafel slope
of 140 mV · dec−1, thus the HER mechanism follows the Volmer path as a rate-determining step ([Figure 2d]). As predicted, Ru@COF-1 showed impressive durability even after 1000 CV cycles,
proving the structural stability of the host and the strong coordination bond among
Ru ions and COF-1.
Figure 2 Design synthesis of noble metal-based Ru@COF-1 HER electrocatalysts. (a) Synthetic
route to COF-1 and Ru@COF-1 composite. (b) N2 adsorption isotherm curves and the pore size distributions of COF-1 and Ru@COF-1.
(c) Linear sweep voltammetry (LSV) curves toward HER of RuCl3, COF-1, and Ru@COF-1. (d) Tafel plot of Ru@COF-1. Reprinted with permission from
Ref. [38]. Copyright 2022 Wiley-VCH.
Incorporation of metal nanoparticles (M NPs) into porous COFs has also been adapted
to diversify COF-based HER electrocatalysts. In particular, covalent triazine frameworks
(CTFs), a class of chemically stable COFs, are attractive hosts for accommodating
metals or M NPs as their triazine (C3N3) units would allow for facile charge transfer and act as additional HER active sites.[58],[59] Hu and team designed a CTFs/MoS2 composite as HER electrocatalysts by in situ growing MoS2 NPs into the pore surface of a CTF.[60] The CTF was prepared via traditional ionothermal synthesis in the presence of ZnCl2 in a vacuum Pyrex tube under N2 atmosphere. The CTF afforded high surface areas as large as 1562.6 m2 · g−1 and a homogeneous pore diameter of 1.1 nm. Subsequently, the CTF was soaked into
a solution containing (NH4)6 Mo7O24.4H2O/CH4N2S and further transferred to hydrothermal treatment to afford CTF/MoS2-X composites with a controlled quantity of NP loading (X = CTF/MoS2 mass ratio = 0.1, 0.2, 0.5, 1, 2, 5, 10). The large surface areas and accessible
pore size lead to the nanosized-to-large NP growth of MoS2 in the pore surface of the CTF, thus exposing more catalytic sulfur edge for HER.[61] Remarkably, the CTFs/MoS2-5 composite with surface areas and pore volume of 131.8 m2 · g−1 and 0.19 cm3 · g−1, respectively, exhibited an overpotential of 93 mV at a current density of 10 mA · cm−1 in an acidic electrolyte (0.5 M H2SO4) for HER, which was much smaller than those of CTFs (409 mV) and free MoS2 (407 mV)-based electrodes. Indeed, the overpotential of CTFs/MoS2-5 was almost comparable to that of the Pt benchmark catalyst (20% Pt/C). This notable
electrocatalysis performances were assumed due the presence of well-arranged 1D channel
arrays allowing effective electron transmission and mass diffusion as well as the
accessibility of MoS2 active sites in the H2 evolution process.
Electron transfer is crucial in the electrocatalytic process. Depositing COFs on conductive
materials (graphene, carbon nanotubes, etc.) could improve the electric conductivity
of the hybrid materials and accelerate the electron transfer. Recently, Liu and team
developed a strategy to better exploit the potential use of COFs as HER electrocatalysts
by growing a chemically stable COF film onto the electrically conductive graphene
oxide (GO) to afford a COF-GO membrane-based electrocatalyst ([Figure 3]).[40] The highly π-conjugated aza-fused BPT-COF was prepared by a liquid-phase method
of a dilute solution containing 2,3,6,7,10,11-triphenylenehexaamine (TPHA) and 2,7-di-tert-butylpyrene-4,5,9,10-tetrone (t-BPT) at room temperature in an open system ([Figure 3a]). This strategy allows for spontaneous polycondensation of both vicinal diamines
and diketones driven by near-equilibrium film growth. Adopting this strategy, a uniform
COF film was in situ assembled with a conducting GO substrate by dissolving a TPHA/GO
mixture and the composite membrane was obtained via vacuum filtration (BTP-COF-GO
hybrid membrane) ([Figure 3b]). This hybrid membrane was then reduced by annealing to obtain conductive BTP-COF-rGO
and further loaded onto a glassy carbon electrode. Remarkably, the BPT-COF-rGO-x membrane (x = mass ratio of GO to TPHA = 1) achieved very small overpotential (45 mV) for HER
at 10 mA · cm−1 in an acidic electrolyte (0.5 M H2SO4), which was better than those of metal-free and metal-based HER electrocatalysts
mentioned earlier and also close to that of the 20% of the commercial Pt/C catalyst
(34 mV) ([Figure 3c]). Furthermore, it exhibited a small Tafel slope of 53 mV · dec−1, which was lower than that of N-doped graphene, thus indicating that the Heyrovsky
reaction is the rate-determining step in the electrocatalytic HER process ([Figure 3d]).[6] Furthermore, BPT-COF-rGO-1 demonstrated efficient charge transfer with very small
resistance (2.5 Ω) according to the Nyquist plot ([Figure 3e]). All these results confirmed the critical role of the chemical and electronic coupling
of both the COF membrane and the conductive rGO substrate. Meanwhile, adopting a similar
strategy, Wang and team reported an elegant strategy by grafting the ruthenium (Ru)-modified
bipyridine-based COF (TpBpy-Ru) on carboxyl-functionalized carbon nanotubes (c-CNTs),
thus enhancing the electron transfer capacity ([Figure 3f]).[39] The c-CNT@TpBpy was firstly prepared via mechanochemical grinding and further immobilizing
the Ru precursor at room temperature. Such a synthetic strategy combines the well-dispersed
HER active Ru species on TpBpy pores and enhanced the electron transfer capacity of
the c-CNT@TpBpy composite. Benefited from the retained crystallinity and porosity,
the c-CNT-0.68@TpBpy-Ru electrode (mass loading 0.5 mg · cm−2) showed excellent HER activity with an overpotential 112 mV (at 10 mA · cm−2) and a remarkable stability for 12 h in 1.0 M KOH, which is superior to those of
most of the reported COF electrocatalysts in alkaline solution.
Figure 3 Design synthesis of COF/conductive substrate composites for enhanced electrocatalytic
HER performance. (a) Schematic illustration of aza-fused BPT-COF synthesis by a solvothermal
or liquid-phase method. (b) Schematic illustration of the fabrication of BPT-COF-GO
electrode. (c) LSV curves of Pt/C, BPT-COF, BPT-COF-rGO-x (x = 0.5, 1, 2, 3), and rGO in 0.5 M H2SO4. (d) The related Tafel plots of BPT-COF-rGO membranes. (e) The Nyquist plots of the
BPT-COF-rGO membranes. Reprinted with permission from Ref. [40]. Copyright 2021 Wiley-VCH. (f) Synthesis route for c-CNT@TpBpy-Ru HER electrocatalyst.
Reprinted with permission from Ref. [39]. Copyright 2023 Wiley-VCH.
So far, all these reported COF-based HER electrocatalysts are promising. However,
their electrocatalytic performances in general are still lower than those of benchmark
catalysts. The poor electrical conductivity and the lower chemical stability, especially
under harsh electrochemical conditions of most of COFs, are the major obstacles for
achieving desirable practical application for water electrolysis.
3.3 COF-Based OER Electrocatalysts
OER, the other half-reaction in a water electrolysis system, has a similar importance
to HER but undergoes at a more complex and sluggish rate. In particular, OER involves
the intervention of multiple protons and electrons, thus metals with variable oxidation
states are necessary as oxygen evolving catalysts.[62] Unfortunately, those metal catalysts particularly suffer from dissociation into
a soluble homogeneous species during the catalytic operation,[63] thus incorporation into a highly stable support is highly necessary. To this end,
COF materials have also been manipulated for electrocatalytic OER due to their prominent
properties for settlement of electroactive metals on the pore surface ([Table 1]).[21],[22] The first effort in realizing COFs for OER was reported by Kurungot and team in
2016, using a cobalt (Co)-containing 2D COF ([Figure 4]).[41] The COF was obtained by Schiff-base condensation of a 1,3,5-trifomylphloroglucinol
(Tp) with 2,2′-bipyridine-5,5′-diamine (Bpy), affording a mesoporous bipyridine-based
TpBpy COF ([Figure 4a]). TpBpy was highly crystalline with a high BET surface area of 1667 m2 · g−1 and 2.1 nm pore size ([Figure 2b, c]). Hence, together with the presence of bipyridine moieties as coordination sites
for metal and decent porosity, TpBpy a was perfect host to accommodate electroactive
Co species. Upon metalation by impregnation with methanolic cobalt acetate, significant
surface area reduction (down to 450 m2 · g−1) and negligible PXRD change were observed, confirming the significant Co–N active
sites in the Co-TpBpy (13 wt% of Co deposited). Notably, the electrode of Co-TpBpy-coated
glassy carbon exhibited an overpotential of 400 mV at 1 mA · cm−2 (calculated to be ~520 mV at 10 mA · cm−2) for OER in a phosphate buffer (neutral pH condition) ([Figure 4d]). More importantly, polarization curve retention was observed even after 1000 cycles,
confirming the good stability of the Co-TpBpy electrode. Furthermore, a Tafel slope
of 59 mV · dec−1 was documented, suggesting possibly that it followed a reversible one-electron transfer
mechanism for OER ([Figure 4e]).[64] It was assumed that these electrocatalytic activities might arise from the synergetic
effect of the inherent porosity and the presence of coordinating units in the COF
skeleton. For the sake of improving mass transport of the O2 bubbles during OER, TpBpy was prepared with a hierarchical macro-microporous architecture
via a hard-template-assisted method using polystyrene sphere (PS) to better access
of the OER active site ([Figure 4f]).[42] This method allows for the formation of crystalline COFs with inherent macroporosity,
thus providing interconnected macropores within the structure (macro-TpBpy) as shown
by scanning electron microscopy (SEM) ([Figure 4g]). In particular, macro-TpBpy managed higher BET surface areas (723 m2 · g−1) relative to the pristine TpBpy (588 m2 · g−1) with preserved pore size, identifying that the macropore efficiently promotes the
accessibility of micropores ([Figure 4h]). Remarkably, upon metalation with cobalt acetate, the macro-TpBpy-Co electrode
(mass loading of 0.25 mg · cm−2) with a surface area of 387 m2 · g−1 demonstrated a significantly improved OER with a small overpotential of 380 mV to
achieve an anodic current density of 10 mA · cm−2, which was much smaller than those of macro-TpBpy and the previously reported Co-TpBpy
with conventional hydrothermal synthesis ([Figure 4i]).[41] Furthermore, it exhibited a Tafel slope of 54 mV · dec−1, smaller than those of macro-TpBpy (339 mV · dec−1), RuO2 (79 mV · dec−1), and the previously reported Co-TpBpy (59 mV · dec−1)[41], thus indicating the favorable reaction kinetics in the OER process ([Figure 4j]). These were assumed due to the homogeneous and interconnected microporous structures
of macro-TpBpy.
Figure 4 The synthesis and electrocatalytic OER activity Co-TpBPy and macro-TpBPy-Co. (a)
Design synthesis of TpBpy and Co-TpBpy via Co (II) impregnation. (b) Comparative PXRD
pattern of TpBpy and Co-TpBpy. (c) The N2 adsorption isotherm of TpBpy and Co-TpBpy. (d) The LSV stability test profile of
Co-TpBpy before and after 1000 cycles (inset shows an enlarged view of the LSV profile).
(e) The Tafel plot of Co-TpBpy at neutral pH. Reprinted with permission from Ref.
[41]. Copyright 2016 American Chemical Society. (f) Schematic representation of macro-TpBpy
fabrication with PSs as a hard template. (g) SEM image of a monodisperse macro-TpBPy.
(h) N2 adsorption−desorption isotherms of the TpBpy and macro-TpBpy. (i,j) OER polarization
curves and the corresponding Tafel plots for macro-TpBpy, macro-TpBpy-Co, TpBpy-Co,
and a commercial RuO2 catalyst. Reprinted with permission from Ref. [42]. Copyright 2019 American Chemical Society.
Adopting similar metal–N as an OER active site, metalloporphyrin with a four coordinated
metal–N4 structure is an attractive OER electrocatalyst; particularly, porphyrin with coordinated
high-/low-valent metal ions enables oxidizing/reducing catalytic cycles.[65],[66] To this regard, metalloporphyrin-based COFs have been designed to enable OER. For
instance, Zeng and team prepared Co-based metalloporphyrin COFs as promising OER electrocatalysts.[43] The COFs were prepared by reacting diarylamine-based 4,4′,4′′,4′′′-(1,4-phenylenebis(azanetriyl))tetrabenzaldehyde
(PATA) or 4,4′,4′′,4′′′-([1,1′-biphenyl]-4,4′-diylbis(azanetriyl)) tetrabenzaldehyde
(BDTA) with 5,10,15,20-tetrakis(4-aminophenyl)porphinato]-cobalt (TAPP(Co)) to afford
CoTAPP-PATA-COF and CoTAPP-BDTA-COF, respectively, via one-step synthesis. In particular,
these arylamines are typical electron donors and redox-active cores,[67],[68] thus they could promote effective electron transport as well as improve the electrochemical
active surface areas in the electrocatalytic process. Hence, both Co-based porphyrin
COFs are attractive electrocatalysts. In addition, CoTAPP-PATA-COF achieved a high
surface area of 943.72 m2 · g−1 with a pore size of 1.1 nm, while higher surface areas (1047.82 m2 · g−1) and large pore size (1.2 nm) were shown by CoTAPP-BDTA-COF. As for one-step synthesis,
Co species were about 3.88 and 3.21 wt% in CoTAPP-PATA-COF and CoTAPP-BDTA-COF, respectively.
More importantly, both COFs are chemically stable even in highly acidic or basic solutions.
Inspired by these prospective properties, both Co–porphyrin COFs were employed as
oxygen-involving electrocatalysts. As for OER in particular, the electrode-based CoTAPP-PATA-COF
(mass loading of 0.2 mg · cm−2) afforded an overpotential of 420 mV at 10 mA · cm−2 current density, which was smaller than that of CoTAPP-BDTA-COF (470 mV). Meanwhile,
a small Tafel slope of 56 and 57 mV · dec−1 was achieved by CoTAPP-PATA-COF and CoTAPP-BDTA-COF, respectively. On the other hand,
higher overpotentials of 670 and 550 mV were observed for both NiTAPP-PATA-COF and
FeTAPP-PATA-COF electrode analogues with similar mass loading (0.2 mg · cm−2), confirming that Co was more reactive for HER than Ni and Fe. Further investigation
revealed that diarylamine units in both COFs played an important role in improving
the electrocatalytic performance. On the other hand, to construct COFs with high density
and openly exposed OER active sites, Peng and team introduced Co–porphyrin onto a
2-fold interpenetrated 3D structure.[44] A highly connective 3D ZJTU-1 COF with stp topology was prepared by condensing 6-connected hexagonal prism (D3 h
) node-based 2,3,6,7,14,15-hexa(4-formylphenyl)triptycene (HFPTP) with 5,10,15,20-tetra
(4-aminophenyl)porphyrin (TAPP) as a perfect support to anchor Co species. Interestingly,
only a slight decrease of surface areas (from 724.97 to 656.89 m2 · g−1) and retained pore size were observed after immobilization of 5.54% of Co metal into
the porphyrin moieties (ZJTU-1@Co). Remarkably, an electrode composed of ZJTU-1@Co
deposited onto a carbon cloth (mass loading of 4 mg · cm−2) in 1 M KOH solution only required an overpotential of 295 mV at 10 mA · cm−2, which was close to the commercial RuO2 (257 mV). Additionally, it exhibited a Tafel slope of 64 mV · dec−1. This report clearly shows that 3D COFs with their open-pore structure show impressive
electrocatalytic performance.
Likewise, phthalocyanine COFs (Pc-COFs) also provide suitable anchor sites for uniformly
deposited metal-based electrocatalysts.[69] Recently, Salonen and co-worker designed a series of metalated imide-linked Pc-COFs
with well-controlled Ni and Fe species as OER electrocatalysts.[45] The H2PcCOF, H2NiPcCOF, and NiPcCOF series were bottom-up prepared by varying the H2Pc/NiPc ratio to link with benzidine, while controlled postsynthetic modification
of the as-synthesized H2PcCOF and H2NiPcCOF with a solution of FeCl2 in DMF, afforded H2FeCOF and H2NiFeCOF series ([Figure 5a]). The resultant COFs showed moderate surface areas (467, 462, 323, 326, and 346 m2 · g−1) with almost similar pore sizes (1.2, 1.3, 1.3, 1.4, and 1.4 nm) for H2PcCOF, H2NiPcCOF, NiPcCOF, H2FePcCOF, and H2NiFePcCOF, respectively. Upon subjecting to the OER electrolysis system, the deposited
COFs onto the Ni foam (mass loading of 3 mg · cm−2) demonstrated notable OER performance, with NiPcCOF achieved the smallest overpotential
of 410 mV (at 10 mA · cm−2) relative to other metalated Pc-COFs (η
10 ≈ 430 mV), while H2PcCOF showed unfavorable overpotential following the Ni foam ([Figure 5b]). Furthermore, the metalated PcCOFs also showed much smaller Tafel slopes (62, 68,
75, and 78 mV · dec−1 for H2FePcCOF, H2NiFePcCOF, NiPcCOF and H2NiFePcCOF, respectively) than H2PcCOF (121 mV · dec−1) and Ni foam (127 mV · dec−1) ([Figure 5c]). More importantly, the COFs showed excellent long-term stability in 1 M NaOH electrolyte
during the tested 100 h ([Figure 5d]). These results suggest that PcCOFs play a crucial role in improving the electrocatalytic
performances and stability of the electrodes. Meanwhile, using different anchoring
sites (i.e., –SO3), the bimetallic NiFe ion was incorporated into 2D COF-SO3 to obtain NixFe1−x@COF-SO3 as promising OER electrocatalysts.[46] Interestingly, the Ni0.5 Fe0.5@COF-SO3-based electrode showed impressive OER performance with a turnover frequency of 0.14 s−1 and a small overpotential of 300 mV at 10 mA · cm−2 as well as a Tafel slope of 83 mV · dec−1. On another occasion, a 2D COF with tetrazole units (COF-TpDb-TZ) was postsynthetically
prepared to accommodate electroactive Co ions to serve as OER electrocatalysts.[47] As predicted, upon metalation, COF-TpDb-TZ-Co only required a overpotential of 390 mV
to achieve a current density of 10 mA · cm−2 in 1 M KOH solution, which was much lower than that of COF-TpDb-TZ. This strengthens
the significant catalytic activity of Co2+. Additionally, it exhibits a Tafel slope of 82 mV · dec−1, much smaller than that of COF-TpDb-TZ (477 mV · dec−1), thus indicating the faster kinetic and improved electrocatalytic performance of
the COF upon metalation.
Figure 5 Design synthesis and electrocatalytic OER performance of metalated Pc-COFs series.
(a) Synthesis route to H2PcCOF and metalated PcCOFs. (b) Anodic polarization curves of H2PcCOF and metalated PcCOF electrodes in 1 M NaOH electrolyte. (c) The Tafel plots
for H2PcCOF and metalated PcCOFs. (d) Chronopotentiometry profiles of H2PcCOF and metalated PcCOFs at 10 mA · cm−2. Reprinted from Ref. [45] published under a creative commons license (CC BY). (e) The schematic diagram of
the fabrication process for Fe-SAC@COF. (f) The aberration-corrected HAADF-STEM images
of Fe-SAC@COF (left) and the corresponding experimental K-edge XANES spectra and the
reference samples (right). (g) The LSV curve comparison of the M-SAC@COF. (h) The
Tafel slope comparison of M-SAC@COF. Reprinted from Ref. [50] published under a creative commons license (CC BY-NC-ND).
COFs with M NPs have also been explored as potential OER electrocatalysts. Vaidhyanathan
and team in 2016 used an imine-linked COF (IISERP-COF2) with highly flexible tetrahedral
sp3 nitrogen in building (tris(4-formylphenyl)-amine) as a perfect support to stabilize
a small size OER active M NP.[48] The highly crystalline IISERP-COF2 managed a high BET surface area of 557 m2 · g−1 and a bimodal pore size of 1.9 and 2.1 nm. The presence of the sp3 nitrogen triazine core and C=N groups in IISERP-COF2 enhanced interaction towards
formation of M NPs. Metalation was performed via the solution route and reduction
to M0 using NaBH4 to afford series of M NPs loaded with 16Ni-COF [1], 16Co-COF [2], 8Co:8Ni-COF [3], 12Co:4Ni-COF [4], and 4Co:12Ni-COF [5], causing almost 71% porosity reduction. An electrocatalytic OER experiment in deaerated
0.1 M KOH with a catalyst mass loading of 20 µg confirmed that the composite 5 exhibited excellent OER electrocatalytic activity with an overpotential of ≈ 258 mV
at 10 mA · cm−2, superior to 3 (315.8 mV), 4 (399.8 mV), 1 (402.3 mV) and 2 (487.3 mV) as well as to all reported OER-based COF electrocatalysts ([Table 1]). Likewise, the composite 5 showed the smallest Tafel slope (39.8 mV · dec−1) compared to 4 (86.3 mV · dec−1), 3 (64.1 mV · dec−1), 2 (94.1 mV · dec−1), and 1 (89.4 mV · dec−1). Employing low band-gap benzimidazole-linked IISERP-COF3 as a support, Vaidhyanathan
and team further deposited Ni3N NP to enhance the electrocatalytic performance of this transition metal catalyst.[49] Such COFs with heterocyclic linkage could drive a low band gap due to the higher
conjugation, thus possessing an ideal electronic support for catalytically active
NPs.[70] IISERP-COF3 was highly porous with a BET surface area of 2022 m2 · g−1 and mesopores of 2.5 nm, hence favoring the growth of metallic Ni3N NPs via nanoscopic confinement (Ni3N-IISERP-COF3). More importantly, the conducting nature of the COF allows electronic
interaction among COF/Ni3N possible. Accordingly, electrodes based on IISERP-COF3 or Ni3N-IISERP-COF3 were prepared by depositing them onto glassy carbon electrodes with
a mass loading of ~0.07 mg · cm−2. Interestingly, Ni3N-IISERP-COF3 with sufficient porosity preservation (~606 m2 · g−1) afforded an overpotential of 230 mV at 10 mA · cm−2, smaller than that of pristine IISERP-COF3 (400 mV) in deaerated 1 M KOH solution.
Additionally, it exhibited a Tafel slop of 79 mV · dec−1. These noticeable electrocatalytic performances were assumed as the COF acted as
a reliable matrix to disperse Ni3N NPs with higher accessibility, thus providing effective charge transport within
the composite. To maximize the atomic-utilization efficiency, an iron single-atom
catalyst (Fe SAC) confined in a 2D COF was realized as a powerful OER electrocatalyst.[50] A 2D COF (Tp-Tta COF) was designed with a suitable coordination pocket to confine
OER active Fe-SAC via unusual Fe–NO atomic arrangement in the skeleton ([Figure 5e]). The Tp-Tta COF was a typical 1 nm honeycomb-like pore COF with a BET surface area
of 716 m2 · g−1 and excellent chemical stability even in alkaline solution. Deposition of Fe-SAC
was performed by mixing the COF with a Fe precursor at low temperature (−60 °C) to
prevent metal aggregation and further reduction treatment with N2H4.H2O to produce the targeted Fe-SAC@COF. This procedure deposited 1.0 wt% Fe-SAC as confirmed
by its TEM image and K-edge XANES spectrum ([Figure 5f]), thus causing reduction of surface areas (down to 470 m2 · g−1) without affecting the pore size. Hence, Fe-SAC@COF is an attractive electrocatalyst.
As predicted, an electrode composed of Fe-SAC@COF (catalyst mass loading up to 1 mg · cm−2) exhibited excellent OER activity with a low overpotential of 290 mV to achieve a
current density of 10 mA · cm−2, which was superior compared with the prepared Fe-NP/COF (359 mV) and pristine Tp-Tta
COF electrode (430 mV) ([Figure 5g]). Additionally, it also outperformed the Ni-SAC@COF analog (337 mV) prepared via
the same procedure. This result was further amplified by its fastest kinetics for
OER proven by its lowest Tafel slope (40 mV · dec−1) among all samples (45, 51, and 129 mV · dec−1 for Ni-SAC@COF, Fe-NP/COF, and Tp-Tta COF, respectively) ([Figure 5h]). This work provides evidence that improving the atomic utilization by means of
SA species improved the electrocatalytic performance.
Although OER is sluggish and thus required metal catalysts, metal-free COFs are also
potential OER electrocatalysts. A new electroactive thiadiazole-based COF (C4-SHz
COF) was developed as a promising OER electrocatalyst by reacting 1,3,5-tris(4-formylphenyl)benzene
with 2,5-dihydrazinyl-1,3,4-thiadiazole.[51] Upon activation with supercritical CO2 treatment, the C4-SHz COF was highly crystalline and composed of a nitrogen-rich
thiadiazole moiety as an OER active site with a BET surface area of 1224 m2 · g−1 and an accessible pore size of mainly 1.85 nm. These properties suggest a potential
electrocatalyst application. Accordingly, the OER activity of a prepared electrode
of C4-SHz COF with a mass loading of 0.07 mg · cm−2 was tested in aqueous 1 M KOH solution. Remarkably, the COF exhibited an onset overpotential
of 250 mV and only required an overpotential of 320 mV to reach a current density
of 10 mA · cm−2, which was lower than that of commercial IrO2/C catalyst. Comparatively, this performance is outstanding in comparison with several
metalated-COF-based OER electrocatalysts mentioned in [Table 1]. Furthermore, it managed a Tafel slope of 39 mV · dec−1, lower than that of IrO2/C (57 mV · dec−1) tested in the same system. Further electrochemical analysis confirmed that this
notable OER performance may associate with the higher charge transfer kinetics and
faster electron transfer process within the structures of the COF. Inspired by our
previous result on tetrathiafulvalene (TTF)-based 3D COFs with excellent electrical
conductivity,[71] our team recently designed a 2D TTF-COF (JUC-630) as a potential metal-free COF
OER electrocatalyst taking advantage of the good electron donor of TTF and thiadiazole
unit as an OER active site. JUC-630 was a mesopore COF with a pore diameter of 2.35 nm
and achieved a surface area of 907 m2 · g−1, thus providing accessibility to the electrocatalytic sites. It was then employed
as an electrocatalyst for water oxidation in aqueous 1 M KOH solution. An overpotential
of 400 mV was required to achieve a current density of 10 mA · cm−2, which was smaller than the overpotential required by Etta-Td (450 mV), a COF analogue
without the TTF unit. This result confirms the crucial role of TTF unit in the OER
performance of the COF. Additionally, it exhibited a Tafel slope of 104 mV · dec−1.
4 Conclusions and Outlook
Owing to their prominent properties such as high crystallinity, superior porosity
with devisable porous architecture and tunable chemical composition and functionality,
COFs have been attractive new-generation electrocatalytic materials, particularly
for water splitting electrocatalysis. COFs offer several benefits in comparison with
traditional electrocatalytic materials, such as controllable heteroatom incorporation
and designed porous architectures, thus enhancing the catalytic performance. The exceptional
structural stability is reinforced by additional supramolecular forces and the complementary
donor/acceptor and redox units, enriching their electronic characters. Furthermore,
COFs provide a suitable platform for incorporating reactive metals via strong coordination
chemistry, resulting in excellent and highly efficient electrocatalysts. These advantages
result in advancement in the employment of COFs as water splitting electrocatalysts.
Among them, noble metals containing COFs have been prepared to improve the selectivity
and stability of the noble metals. Meanwhile, in terms of low cost and decent electrocatalytic
performance, non-noble metal/COF electrocatalysts, including dual transition metals
and SAC-containing COFs, have been widely explored as promising electrocatalysts.
Nevertheless, metal-free COFs have also been screened recently, envisioning a green
and sustainable approach for water splitting technology.
Although some progresses have been seen, the research of COFs in this field is still
in its infancy. Thus, there are still lot of gaps for improvements. Certainly, some
challenges are there to be addressed for the sake of efficient water splitting electrocatalysis.
Generally, COFs are less conductive, thus it is highly important to optimize the conductivity
by means of specific design of COF structure, such as with a donor–acceptor configuration.
In the case of durability, COF-based electrocatalysts shall be highly resistant toward
harsh environments (e.g., in strong acidic and basic systems). This could be tackled
by employing COFs with stable linkages or introduction of supramolecular enforcement
within the structure. Meanwhile, most of those COF electrocatalysts are dominated
by 2D COF structures, which are likely to suffer from ineffective active site utilization
due to the highly layer stacking. 3D COF electrocatalysts shall provide an efficient
platform with 3D open-pore structures and higher surface areas. Despite highly significant
to boost the electrocatalytic activity, development of single-atom-based water splitting
electrocatalysts is still rare. Designing COFs with specific coordination pockets
has been seen to enable the controlled nucleation of single-atom species. Furthermore,
development of dual HER/OER electrocatalyst-based COFs is unseen and yet challenging
to realize. A rational design of such electrocatalysts is highly in demand to promote
full water splitting electrocatalysis. Nevertheless, the use of thin film or membrane-based
COFs, instead of commonly prepared crystalline powder, provides convenience for integration
into the device. Finally, the role of COFs in the catalytic process is still unclear.
Thus, it is highly important to get insight into the active site and chemical kinetics
at the molecular level. In summary, by addressing all these synthetic and practical
challenges, COF-based electrocatalysts would be highly promising for the development
of efficient and low-cost water splitting technology.
Funding Information
This work was supported by the National Key R&D Program of China (2021YFF0 500 504
and 2022YFB3 704 900), the National Natural Science Foundation of China (22 025 504,
21 621 001, and 22 105 082), the SINOPEC Research Institute of Petroleum Processing,
“111” project (BP0719036 and B17020), and the program for JLU Science and Technology
Innovative Research Team. Y. Y. and F. C. thank Jilin University “Dingxin Scholar
Program” for the financial support.