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Supporting Information
Carbon Nitride Embedded with Transition Metals for Selective
Electrocatalytic CO2 Reduction
Chunmei Ding,a, # Chengcheng Feng,b, # Yuhan Mei,c Fengyuan Liu,d Hong Wang,a Michel
Dupuis,a,c Can Lia,*
a State Key Laboratory of Catalysis, Dalian Institute of Chemical Physics, Chinese Academy
of Sciences; Dalian National Laboratory for Clean Energy, Dalian 116023, China.
b School of Chemistry and Materials Science, University of Science and Technology of China,
Hefei 230026, China
c Department of Chemical and Biological Engineering and Computation and Data-Enabled
Science and Engineering Program, University at Buffalo, State University of New York,
Buffalo, New York, USA.
d State Key Laboratory of Fine Chemicals, Zhang Dayu School of Chemistry, Dalian
University of Technology, Dalian 116023, China
1
1. Synthesis of Materials
All chemicals were analytical grade and were used as purchased without further
purification. The details are as follows: NiCl2·6H2O (98%, Tianjin Kemiou Chemical Reagent
Co., China), CuCl2·2H2O (98%, Sinopharm, China), MnCl2·4H2O (98%, Sinopharm, China),
dicyandiamide (Sinopharm, China), CO2 gas (> 99.999%, Guangming, Dalian, China).
Multiwall carbon nanotubes (CNT, TIME NANO, Chengdu, China) were pretreated
before use. Typically, 4 g CNT was dispersed in 200 mL HNO3 (65~68 wt.%) and refluxed at
140 oC for 13 h. After cooling down, the above mixture was transfered to 250 mL water, and
then cooled to room temperature. Then the suspension was filtered and washed to neutral pH.
The product was dried at 65 oC and grinded.
Metal-C3N4-CNT catalysts with various transition metals were synthesized with a
method modified from that previously reported.[1] Based on theoretical predictions, one
triazine (C6N8) or two g-C3N4 moieties can coordinate one metal atom. Therefore, it was
expected that 3 mol dicyandiamide can coordinate 1 mol metal ions. Based on this
assumption, firstly, 25 mg of treated CNT was dispersed in 100 mL water. Then 50 mg
dicyandiamide and 0.1 mmol of metal precursor were added and stirred for 20 h at 50 oC.
Note that the amount of dicyandiamide was doubled to ensure coordination efficiency and to
also account for melamine sublimation during the polymerisation of g-C3N4 from
dicyandiamide. The mixture was then dried in vacuum at 55 oC and the collection was
annealed at 600 oC in N2 with a flow rate of 50 mL min-1. The product was subsequently
stirred in 1 M HCl for 10 h to remove the metal and metal oxides, and then washed with large
amount of water several times. The C3N4-CNT was prepared by the same procedure without
the addition of metal precursor, and pristine C3N4 was synthesized by annealing
dicyandiamide precursor directly in N2. Metal-CNT was synthesized similarly without
dicyandiamide. Metal-N/CNT was prepared by annealing the metal-C3N4-CNT at 900 oC in N2
for 2 h.
2
The electrode was prepared by drop casting the catalyst ink on C paper (Toray, H060).
The ink was a mixture of 2 mg catalyst, 60 μL water, 90 μL ethanol and 50 μL nafion solution
(1 wt.% in ethanol), ultrasonically dispersed for 30 min. The loading amount of the catalyst
was 1 mg cm-2.
2. Physical characterizations
The morphologies were examinzed by transmission electron microscopy (TEM, Hitachi
HT7700) and high resolution transmission electron microscopy (HRTEM, JEOL JEM-
2000EX). The high angle annular dark field scaning transmission electron microscopy
(HAADF-STEM) images were taken on a probe-corrected JEM-ARM200F electron
microscope. Compositional maps were acquired with an energy dispersive X-ray spectrometer
(EDS) fitted on the microscope. X-ray photoelectron spectroscopy (XPS) measurements were
performed using a Thermofisher ESCALAB 250Xi spectrometer with Monochromated Al Kα
excitation (1486.6 eV, 15 kV, 10.8 mA). The Raman spectra was detected on a RENISHAW
inVia Raman Microscope with 532 nm laser (2.25 mW) with a scan time of 60 s.
For the elemental ICP measurements (ICP-OES, PerkinElmer, 7300DV), 25 mg sample was
put into a quartz boat and treated in air at 700 oC for 6 h in a muffle oven. The solid collection
was dissolved by 4 mL of concentrated acid.
3. Electrochemical measurements
Electrochemical measurements were conducted in a three-electrode setup with Pt counter
electrode (2 cm × 3 cm) and SCE reference electrode. Otherwise mentioned, all potentials
were controlled by a potentiostat (CHI 660e) without iR compensation and were converted to
reversible hydrogen electrode (RHE) scale using E (V vs. RHE) = E (V vs. Ag/AgCl) +
0.1976 V + 0.059* pH. The pH values of 0.5 M KHCO3 saturated with Ar and CO2 are 8.3
and 7.5, respectively. The selectivity and reaction rate of CO2RR were evaluated by
controlled-potential electrolysis in an H-type cell containing 0.5 M KHCO3 electrolyte with a
Nafion-117 membrane. Electrolytes were pre-saturated and bubbled with CO2 during
3
measurements. CO evolution rate was determined by an online gas chromatograph (GC,
Agilent 7890, Ar carrier and TDX-01 packed column) equipped with TCD (for H2 detection),
FID detectors and a methanizer (for CO detection). The gas flows though the cell at a constant
flow and was vented into the sampling loop of the GC. A video of CO2 reduction at -0.8 V vs.
RHE with NiCu-C3N4-CNT catalyst was recorded (Movie S1).
The relative electrochemical surface area is determined by the double-layer capacitances
calculated from the plot of discharging current densities vs. scan rates.[2, 3] The cyclic
voltammetry was measured in 0.5 M KHCO3 saturated with CO2 within a none-faradaic
potential region (0.8 V to 0.5 V vs. RHE). Three cycles are recorded at each scan rate and the
current values were taken during the second cathodic scan at 0.65 V. To note that, the relative
electrochemical surface area estimated from the double layer capacity current includes the
contribution of the exposed C substrate.
4. Computational details
4.1. Methods and models
We performed density functional theory (DFT) calculations using a basis set of plane waves
to describe the electron density in conjunction with the projector augmented wave (PAW)
pseudopotentials to represent the 1s core electrons of C and N, and the 1s, 2s, 2p, 3s core
electrons of the transition metal atoms, and with the PBE functional as the energy functional
of the electron density, as implemented in the Vienna ab initio Simulation Package (VASP).
[4-10] The plane wave energy cutoff was set to 550 eV for all metal-C3N4 systems. To note
that, the C3N4 model for DFT calculation is single layer for simplicity. A Gaussian smearing
of 0.01 eV for molecules and 0.2 eV for metal-C3N4 systems was applied for total energy
computations during geometry optimization. The convergence criterion for the self-
consistent-field (SCF) energy calculations was set to be 10-7 eV, and that 0.01 eV/ Å for
geometry optimization. The Bloch representation of the periodic one-electron states were
calculated using the Monkhorst−Pack k-point grid of 2 × 2 × 1 for metal-C3N4 system. For
4
molecules, only the gamma point was sampled. Supercells for energy calculations were
constructed with a 20 Å vacuum layer separation in the z direction to prevent interactions
between the periodic images for metal-C3N4 systems. For molecules, a 20 Å × 20 Å × 20 Å
box was used for simulations. Solvation effects were considered for all systems by simulating
the aqueous environment via a polarizable continuum (with a dielectric constant ε = 80 for
water) surrounding the molecule or the surface atoms as an ‘implicit’ model of solvation as
implemented in VASPsol.[11, 12]
4.2. Energy calculation CO2 activation
The catalytic activity of the carbon-based structures was determined from the binding
energies of the reaction intermediates (i.e., *H, *COOH) to the active site in their lowest
energy conformation following the methodology of Cheng et al.[13] And the overpotential of
the CO2 reduction reaction in these systems determined from the first hydrogenation step to
form *COOH or *OCHO.[14] Thus we investigated here the adsorption and activation energy
of CO2 on different metal-C3N4 structures (Table S3). As mentioned above, CO2 is adsorbed
on the first layer of the C3N4 for the calculation. The reaction process was shown as equation
(1) with ‘*’ denoting the bare system with the active site:
* + H+ + e- + CO2 → *COOH (1)
To interpret the energy data calculated for the various intermediates, we used the
computational standard hydrogen electrode (SHE) model proposed by Nørskov et al.[15] to
calculate potential (E) and pH-dependent free-energies. We report here the data for E = 0 V
versus SHE and pH = 0. The reaction energies of the intermediates were calculated and
corrected for zero-point energy (ZPE), enthalpy correction, entropy correction, and solvation
effects to obtain the reaction free energies (ΔG) according to equation (2) and (3). We used
the ZPE and thermodynamic corrections for the metal-C3N4 system reported by Cheng et al.
for their metal-porphyrin-graphene systems[13] as shown in Table S5.
ΔE = E(ads*) -E(ads) - E(*) (2)
5
ΔG = ΔEsol + ΔH + ΔZPE – TΔS (3)
292 288 284 280
Raw data Peak sum O-C=O 291 C-OH 285.8 C=C 284.6 Background
Cou
nts/
s
Eb / eV
NiMn-CNT C 1s
292 288 284 280
Raw data Peak sum O-C=O 291 C-OH 285.8 C=C 284.6 background
Cou
nts/
s
Eb / eV
NiCu-CNT C 1s
292 288 284 280
Raw Intensity Peak sum O-C=O 291 N=C-N 288.7 C-OH 285.8 C=C 284.6 Background
Cou
nts/
s
Eb / eV
NiMn-C3N4-CNT C 1s
292 288 284 280
Raw data Peak sum O-C=O 291 N=C-N 288.7 C-OH 285.8 C=C 284.6 Background
Cou
nts/
sEb / eV
NiCu-C3N4-CNT C 1s(a) (b)
(c) (d)
Figure S1. High resolution C 1s XPS spectra of (a) NiMn-C3N4-CNT, (b) NiCu-C3N4-CNT,
(c) NiMn-CNT and (d) NiCu-CNT catalysts. All signals are calibrated by C 1s (284.6 eV).
Typical C species of triazine rings (N=C-N, 288.7 eV) can be observed on samples with
C3N4. All the samples show signals of C=C (284.6 eV) from CNTs, oxidized carbon species
C-OH (285.8 eV) and O-C=O (291 eV).
6
408 404 400 396
NiMn-C3N4-CNT Raw data Peak sum C=N-C triazine 398.6 N-(C)3 399.8 N-H 401.3 Background
Cou
nts/
s
Eb / eV
N 1s
408 404 400 396
NiCu-C3N4-CNT Raw Intensity Peak sum C=N-C triazine 398.6 N-(C)3 399.8 N-H 401.3 Background
Cou
nts/
s
Eb / eV
N 1s
(c) (d)
408 404 400 396
C3N4-CNT Raw data Peak sum C=N-C triazine 398.6 N-(C)3 399.8 N-H 401.3 Background
Cou
nts/
s
Eb / eV
N 1s
540 520 400 360 320 280
NiCu-CNT
NiCu-C3N4-CNT
C 1s
N 1s
Cou
nts/
s
Eb /eV
O 1s
NiMn-C3N4-CNT
NiMn-CNT
(a) (b)
Figure S2. (a) The C 1s, N 1s, and O 1s XPS spectra of (NiMn, NiCu)-C3N4-CNT and
(NiMn, NiCu)-CNT catalysts. The high resolution N 1s XPS spectra of (b) C3N4-CNT, (c)
NiMn-C3N4-CNT and (d) NiCu-C3N4-CNT catalysts. The binding energies are calibrated by C
1s (284.6 eV).
The N 1s signals are only observed on samples containing C3N4, which display three typical
N species of g-C3N4 (C=N-C triazine rings at 398.6 eV, N-(C)3 tertiary nitrogen at 399.8 eV,
and N-H amino groups at 401.3 eV). The modification of C3N4-CNT with metal species in the
triazine matrix may have little influence on the texture property of C3N4-CNT. As emphasized
in the main text, there is indeed chemical interaction between N and metal atoms, forming M-
Nx structures. Comparing the N 1s XPS spectra of C3N4-CNT and (NiMn, NiCu)-C3N4-CNT,
the binding energies of N 1s show no changes after metal modification, that’s because the
7
amount of metal species may be too low to cause obvious shift of the binding energy of N
species.
1200 1400 1600 1800 2000
C3N4-CNT
NiCu-C3N4-CNT
NiMn-C3N4-CNT
NiCu-CNT
CNT
NiMn-CNT
1.55
1.18
1.28
1.21
1.35
1.38
1607
1576 G
Inte
nsity
/a.u
.
Raman shift/ nm-1
1343 D
ID/IG
Figure S3. Raman spectra of CNT, C3N4-CNT, NiMn-CNT, NiCu-CNT, NiMn-C3N4-CNT
and NiCu-C3N4-CNT catalysts.
During the pretreatment of CNTs under strong acid condition, there will be many defects on
oxidized CNTs, the Raman spectra shows that the ratio of D-band (disorder of the graphite
carbon) and G-band (presence of crystalline graphitic carbon) is obvious decreased, indicating
that disorder and defects of the graphite carbon is restored during the polycondensation
process of g-C3N4. In addition, there is little change in the ratio of ID/IG, indicating the
introduction of metal species show negligible influence on the texture property of C3N4-CNT.
8
(a) (b)
(c) (d)
100 nm 100 nm
100 nm 100 nm
Figure S4. The TEM images of NiMn-C3N4-CNT (a: without washing; b: washed in 1 M HCl
for 12 h) and NiCu-C3N4-CNT (c: without washing; d: washed in 1 M HCl for 12 h) catalysts
There are many nanoparticles before being washed in acid. However, there are negligible
metal nanoparticles in the catalyst after acid treatment, indicating the metal or metal oxide
nanoparticles are removed. Thus, the CO2RR activity is contributed by metal species
embedded in C3N4-CNT instead of metal or metal oxide nanoparticles.
9
Figure S5. The element mapping results of NiCu-C3N4-CNT catalyst (a) microscopic
image, (b) C element, (c) O element, and (d) Ni element.
Although the background noise of Ni is strong, the element mapping images show that the
Ni element is uniformly distributed on the surface of CNT. Higher density of Ni element
signals can be observed in areas with C and O elements, indicated by the yellow lines.
Table S1. The loading amount of metal elements of (NiCu, NiMn)-C3N4-CNT samples (all
have been washed by acid) determined by ICP measurements
SamplesNi
(wt.%)
Cu
(wt.%)
Mn
(wt.%)
Ni
(μmol cm-2)
Cu
(μmol cm-2)
Mn
(μmol cm-2)
NiCu-C3N4-CNT 6.657 2.079 1.119 0.3271
NiMn-C3N4-CNT 9.188 2.175 1.565 0.3959
10
potentiostat
CE WE
CO
CO2
H+
RE
CO2 CO
Nafion-117stir
Figure S6. A schematic description of the H-type CO2 reduction electrochemical cell
-1.0 -0.8 -0.6 -0.4 -0.2 0.0-40
-30
-20
-10
0
Cu-C3N4-CNT
Ar CO2
J/ (m
A c
m-2)
E vs. RHE/ V-1.0 -0.8 -0.6 -0.4 -0.2 0.0
-50
-40
-30
-20
-10
0
Ni-C3N4-CNT
Ar CO2
J/ (m
A c
m-2)
E vs. RHE/ V
(a) (b)
(c)
-1.0 -0.8 -0.6 -0.4 -0.2 0.0
-40
-30
-20
-10
0
Ar CO2
Mn-C3N4-CNT
J/ (m
A c
m-2)
E vs. RHE/ V
-1.0 -0.8 -0.6 -0.4 -0.2 0.0-80
-60
-40
-20
0
Co-C3N4-CNT
Ar CO2
J/ (m
A c
m-2)
E vs. RHE/ V
-1.0 -0.8 -0.6 -0.4 -0.2 0.0-40
-30
-20
-10
0
Fe-C3N4-CNT
Ar CO2
J/ (m
A c
m-2)
E vs. RHE/ V
(d)
(e)
Figure S7. The LSV scans of M-C3N4-CNT (M = (a) Ni, (b) Cu, (c) Mn, (d) Fe, and (e) Co)
in 0.5 M KHCO3 saturated with Ar (dash) or CO2 (solid)
11
-1.0 -0.9 -0.8 -0.7 -0.6 -0.50
100
200
300
400NiMn-C
3N
4-CNT
Ar
P
rodu
cts/
(m
ol c
m-2 h
-1)
H2 CO
E vs. RHE/ V-1.0 -0.9 -0.8 -0.7 -0.6 -0.5
0
200
400
600
Evs. RHE/ V
NiCu-C3N
4-CNT
Ar
Pro
duct
s/ (
mol
cm
-2 h
-1)
H2 CO
(a) (b)
-0.6 -0.7 -0.8 -0.9 -1.00
20
40
60
80
100
NiMn-C3N
4-CNT
CO2
total CO H
2 F /%
E vs. RHE/ V-0.6 -0.7 -0.8 -0.9 -1.0
0
20
40
60
80
100
NiCu-C3N
4-CNT
CO2
total CO H
2
F/ %
E vs. RHE/ V
(c) (d)
Figure S8. The activity of (a) NiMn-C3N4-CNT and (b) NiCu-C3N4-CNT catalysts in 0.5 M
KHCO3 saturated with Ar. The ηF of CO and hydrogen evolution of (c) NiMn-C3N4-CNT and
(d) NiCu-C3N4-CNT at different potentials in 0.5 M KHCO3 saturated with CO2.
12
-1.0 -0.9 -0.8 -0.7 -0.6 -0.540
60
80
100
NiCu 4:1 NiCu 9:1 NiCu 1:1
F(C
O)/
%
E vs. RHE/ V
-1.0 -0.9 -0.8 -0.7 -0.6 -0.50
200
400
NiCu 4:1 NiCu 9:1 NiCu 1:1
CO
/ (m
ol c
m-2 h
-1)
E vs. RHE/ V
(a) (b)
(c) (d)
-1.0 -0.9 -0.8 -0.7 -0.6 -0.540
60
80
100
NiMn 4:1 NiMn 9:1 NiMn 1:1
F(C
O)/
%
E vs. RHE/ V
-1.0 -0.9 -0.8 -0.7 -0.6 -0.50
100
200
300
400
NiMn 4:1 NiMn 9:1 NiMn 1:1
CO
/ (m
ol c
m-2 h
-1)
E vs. RHE/ V
-1.0 -0.8 -0.6 -0.4 -0.2 0.0-40
-30
-20
-10
0
NiCu 4:1-Ar NiCu 4:1-CO2
NiCu 1:1-Ar NiCu 1:1-CO2
NiCu 9:1-Ar NiCu 9:1-CO2
J/ (m
A c
m-2)
E vs. RHE/ V-1.0 -0.8 -0.6 -0.4 -0.2 0.0
-40
-30
-20
-10
0
NiMn 4:1-Ar NiMn 4:1-CO2
NiMn 1:1-Ar NiMn 1:1-CO2
NiMn 9:1-Ar NiMn 9:1-CO2
J/ (m
A c
m-2)
E vs. RHE/ V
(e) (f)
Figure S9. The (a, b) ηF(CO) and (c, d) CO evolution rates of NiMn-C3N4-CNT and NiCu-
C3N4-CNT catalysts with different Ni:Mn and Ni:Cu ratios in 0.5 M KHCO3 saturated with
CO2. (e, f) The LSV currents of NiMn-C3N4-CNT and NiCu-C3N4-CNT catalysts with
different Ni:Mn and Ni:Cu ratios in 0.5 M KHCO3 saturated with CO2 and Ar.
The highest ηF(CO) and CO evolution rate were obtained with the ratios of Ni:Mn and
Ni:Cu of around 4:1. The ηF(CO) firstly increases with the increase of overpotential and then
decreases, demonstrating the highest ηF(CO) at around -0.8 V vs. RHE. The CO evolution
rates increase with the applied bias.
13
0 20 40 60 80 1000
1
2
3 Ni-C3N4-CNT Mn-C3N4-CNT Cu-C3N4-CNT NiCu-C3N4-CNT NiMn-C3N4-CNT C3N4-CNT
J (c
apac
itive
)/ (m
A c
m-2)
Scan rate/ (mV s-1)
(a)
0 20 40 60 80 1000
1
2
3 NiCu-C3N4-CNT-without washing NiMn-C3N4-CNT-without washing NiCu-C3N4-CNT NiMn-C3N4-CNT
J/ (m
A c
m-2)
Scan rate/ (mV s-1)
(b)
Figure S10 The capacitive current density of different catalysts in 0.5 M KHCO3 as a
function of scan rate over a non-faradic potential range.
Table S2 The relative electrochemical active surface area calculated from the slope of
capacitive current density vs. scan rate in Figure S10.
Relative electrochemical active surface area
Ni-C3N4-CNT 3.9
Cu-C3N4-CNT 3.8
Mn-C3N4-CNT 4.3
NiCu-C3N4-CNT 1.0
NiMn-C3N4-CNT 1.4
C3N4-CNT 2.7
NiCu-C3N4-CNT-without acid treatment 2.0
NiMn-C3N4-CNT-without acid treatment 3.6
14
(d)
(a’) (b’) (c’)
(d’)
(a) (b) (c)
(a’’) (b’’) (c’’)
(d’’)
(e)
(e’)
(e’’)
1.921.91
2.19
1.881.96
2.052.14
2.07
1.881.94
2.082.00
1.97
2.97 3.362.74
2.93 2.11
2.76 2.312.342.16
2.35 2.76
2.31
2.25
2.24
2.29
2.572.82
Figure S11. The optimized structures of mono-metal (a, a’, a’’) Ni-C3N4, (b, b’, b’’) Cu-C3N4,
(c, c’, c’’) Mn-C3N4, bi-metal (d, d’, d’’) NiMn-C3N4 and (e, e’, e’’) NiCu-C3N4 units from
different views. Coloring scheme: blue (N atoms), gray (C atoms), yellow (Ni atoms), green
(Cu atoms) and purple (Mn atoms).
Different coordination structures are formed because the different electronic properties of
metal atoms. For bimetallic systems, the metal atoms seem to be out of the g-C3N4 planar
because of the repulsing interaction of two metal atoms.
15
Table S3. The first-step reaction free energies of (H+ + e- + CO2) forming *COOH on
different structures obtained by DFT calculation
Structure ΔG*COOH
Mn-C3N4 0.97
Ni-C3N4 0.61
Cu-C3N4 0.37
NiCu-C3N4 -0.77
NiMn-C3N4 -1.16
Table S3 shows that the reaction free energies change ΔG*COOH for (Ni, Cu, Mn)-C3N4 are
all positive value, but the values are negative for (NiCu, NiMn)-C3N4 bimetallic catalysts.
That means the reaction (H+ + e- + CO2) forming *COOH changes from endothermic reaction
for mono-metal catalysts to exergonic reaction for bimetallic catalysts.
16
880 870 860 850
10000
15000
20000Ni 2p 855.2
855.3
872.8
872.7
Cou
nts/
s
Eb/ eV
872.5
855.1
Ni-C3N4-CNT
NiCu(4:1)-C3N4-CNT
NiCu(1:1)-C3N4-CNT
880 870 860 8508000
16000
24000 Ni 2p
Ni-C3N4-CNT
NiMn(1:1)-C3N4-CNT
855.3
855.4
872.9
872.8
Cou
nts/
s
Eb/ eV
NiMn(4:1)-C3N4-CNT
872.5 855.1
960 950 940 9308000
10000
12000Cu 2p
932.3
932.3
952.3
952.3
Cou
nts/
s
Eb/ eV
951.3
932.1
NiCu(4:1)-C3N4-CNT
NiCu(1:1)-C3N4-CNT
Cu-C3N4-CNT
660 650 640
10000
12000
14000Mn 2p
643
643
Cou
nts/
s
Eb/ eV
641.7
Mn-C3N4-CNT
NiMn(4:1)-C3N4-CNT
NiMn(1:1)-C3N4-CNT
(a) (b)
(c) (d)
Figure S12. The (a, b) Ni 2p, (c) Cu 2p, and (d) Mn 2p XPS spectra of (NiMn, NiCu)-C3N4-
CNT and (Ni, Cu, Mn)-CNT catalysts. Eb is calibrated with C 1s (284.6 eV).
The binding energies of Ni 2p, Mn 2p and Cu 2p in (NiMn, NiCu)-C 3N4-CNT are shifted to
higher values by about 0.1 eV ~ 0.3 eV compared with those in mono-metal materials,
because the introduction of a second metal element may influence the electronic structures of
the neighboring metal centers.
17
-1.0 -0.8 -0.6 -0.4 -0.2 0.0
-30
-20
-10
0
J/ (m
A c
m-2)
E vs. RHE/ V
CNT-ArCNT-CO2
NiMn-CNT-ArNiMn-CNT-CO2
NiCu-CNT-ArNiCu-CNT-CO2
-1.0 -0.8 -0.6 -0.4 -0.2 0.0-30
-20
-10
0
C3N4-CNT
J/ (m
A c
m-2)
E vs. RHE/ V
ArCO2
(a) (b)
Figure S13. The LSV scans of the (a) C3N4-CNT electrodes and (b) those without C3N4 in 0.5
M KHCO3 saturated with Ar (dash) or CO2 (solid).
-0.6 -0.7 -0.8 -0.9 -1.00
20
40
60
80
100
F C
O /
%
E vs. RHE/ V
C3N4-CNT Ni-C3N4-CNT Mn-C3N4-CNT Cu-C3N4-CNT
C3N4-CNT
Ni-C3N4-CNT
Mn-C3N4-CNT
Cu-C3N4-CNT0
100
200
300
COH
2
Pro
duct
s/ (
mol
cm
-2 h
-1)
(a) (b)
Figure S14. (a) The Faradic efficiency (ηF) of CO evolution at different potentials, (b)
hydrogen and CO evolution rates at -0.8 V vs. RHE on C3N4-CNT and M-C3N4-CNT (M = Ni,
Mn, Cu) catalysts in 0.5 M KHCO3 saturated with CO2.
18
(a) (b)
-1.0 -0.8 -0.640
60
80
100
NiMn-washedNiMn-without washingNiCu-washedNiCu-without washing
F(C
O)/
%
E vs. RHE/ V
0
100
200
300
NiMnwithoutwashing
NiMnwashed
COH
2
Pro
duct
s/ (m
ol c
m-2 h
-1)
NiCuwashed
NiCuwithoutwashing
Figure S15. (a) The hydrogen and CO evolution rates at -0.8 V vs. RHE and (b) the Faradic
efficiency (ηF) of CO evolution at different potentials in 0.5 M KHCO3 saturated with CO2 on
(NiCu, NiMn)-C3N4-CNT catalysts and those without being washed in acid.
(a) (b)
0.0 0.5 1.0 1.50
50
100
150
e/2 CO H
2
-0.5V
Pro
duct
s/(
mol
h-1cm
-2)
Time/h
-0.6VNiMn-C
3N
4-CNT
0.0 0.5 1.0 1.50
50
100
150
e/2 CO H
2
NiCu-C3N4-CNT
-0.5 V
-0.8V
Pro
duct
s/(
mol
h-1cm
-2)
Time/h
-0.6 V
Figure S16. (c) The time-course CO and H2 evolution rates, and the corresponding amount of
e/2 calculated from the current with (c) NiMn-C3N4-CNT and (d) NiCu-C3N4-CNT catalysts at
-0.5 V and -0.6 V vs. RHE and -in 0.5 M KHCO3 saturated with CO2.
19
Table S4 Comparison of the results of this work and those in literatures.
MaterialsMaximu
m ηF(CO)
JCO/ (mA cm-2) at potentials
(vs. RHE) of maximum ηF(CO)
Author, Ref.
No. in main text
(NiCu, NiMn)-C3N4-CNT 90% 15.8 at -0.8 V This work
Ni-N-C 85% 8 at -0.75 V Wen, [36]
single atom Ni-NSG 97% 22 at -0.72 V Yang, [40]
Ni-N-C 93% 3.5 at -0.67 V Hu, [41]
single atom Ni -NCNTs 91.3% 23.5 at -0.7 V Cheng, [49]
Coordinatively
unsaturated Ni-N-C98% 57.5 at -0.83 V Yan, [50]
Co-N2-C 94% 17 at -0.63 V Wang, [52]
Co-N5-C 99% 4.5 at -0.73 V Pan, [53]
Fe-N-C 93% 2.8 at -0.58V Pan, [54]
Co single atom-N/C 82% 10.8 at -0.8 V Geng, [55]
Ni single atom-NCNTs 95% 54 at -1 V Lu, [56]
Ni single atom-GO 92% 26.8 at -0.7 V Cheng, [57]
Ni-N-C 96% 7.5 at -0.75 V Pan, [58]
Table S5. ZPE and thermodynamic corrections in eV’s for CO2RR species and intermediates
Species ΔH + ZPE T×∆S
CO2 0.43 0.66
*COOH 0.72 0.24
*OCHO 0.71 0.24
* 0.00 0.00
20
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