Angewandte
Research Articles
Chemie
[19]
type cell, in which H O acted as a proton source. Under the
frequency data (Figure S24). At OCP, it showed that the
2
reaction conditions, no obvious liquid products were detected
by NMR spectroscopy, and H , CO, CH , C H were the
film resistance (R ) between the catalyst and substrate in the
Cu/PANI-CP (I) electrode was much smaller than that in the
Cu/PANI-CP (II, III). Moreover, the charge transfer resist-
f
2
4
2
4
gaseous products determined using gas chromatography (GC;
Figures S10 and S11). Clearly, Cu/PANI-CP (I) had much
higher FE of C H than other catalysts at all applied potentials
ance (R ) between the electrolyte and Cu/PANI-CP (I)
ct
surface was also much smaller than that of Cu/PANI-CP (II,
2
4
(
Figures S12–S15). The applied potential over the Cu/PANI-
III; Figure S23, Table S2). The smaller R and R result in the
f
ct
CP (I) was much lower, and the partial current density was
much higher. Figure S16 shows the total current density and
partial current density j(C H ) of different catalysts. A partial
lower onset potential and applied potential. Analogously, the
same trends appear in R and R at CO equilibrium potential
f
ct
2
(Figure 4A, Table S3). A reasonable interpretation of the
result is that the introduction of defects in Cu(vacancy)/PANI can
enhance electron mobility and accelerate the charge transfer
rate on Cu/PANI-CP (I) interface (Figure 4C–E, Figur-
2
4
À2
current density j(C H ) of 18.0 mAcm was achieved for Cu/
2
4
PANI-CP (I), which is about 2.2 times that of the Cu-CP (IV)
catalyst. At the applied potential of À1.2 V versus RHE, the
À2
[20]
current density over Cu/PANI-CP (I) can reach 30.2 mAcm
es S25–S28). Therefore, from the bulk to the surface, Cu/
with a C H FE of 59.4% (Figure 3B). For Cu/PANI-CP (II
PANI-CP (I) shows easier electron transfer than other Cu/
PANI interfaces (Cu/PANI-CP (II, III)) (Figure 4F), which is
conducive to enhance the activity of CO RR (Figure 3B).
2
2
4
and III), the FEs for C H were only 24.4% and 31.3%,
2
4
[21]
respectively. The performance of Cu/PANI-CP (I) is further
compared with other state-of-the-art electrocatalysts in
aqueous electrolyte, indicating that its performance is among
the best ones (Supplementary Table 1). Long-term electrol-
ysis was also performed to verify the stability of the catalysts.
Third, Cdl study reveals that the 3D hierarchical structure of
[
22]
Cu/PANI-CP (I) facilities CO diffusion (Figure 3A). From
2
Bode plots, the decrease of modulus of the impedance (log Z)
and moving of the phase angle (f) to higher-frequency region
of Cu/PANI-CP (I) indicates that more electrolyte penetrates
into the pores, which is conducive to CO2 diffusion and
As shown in Figure 3C, the CO RR activity over Cu/PANI-
2
CP (II and III) and Cu-CP (IV) decayed gradually with time
[23]
of CO electrolysis. In contrast, the FE and current density of
provides more opportunity for the reaction (Figure 4B,F),
which favors both the activity and selectivity.
2
Cu/PANI-CP (I) did not change obviously during the
reduction process (Figure 3C, Figure S17). After the reaction,
the morphology of Cu/PANI-CP (I) was well preserved, and
the composition did not change noticeably (Figures S18–S22).
It indicates that the remarkable stability of Cu/PANI-CP (I)
results mainly from the 3D hierarchical structure of the
catalyst. The highly dispersed Cu on PANI prevents agglom-
eration, which have better stability than other catalysts. All
these results illustrated that Cu/PANI-CP (I) have higher
ECSA, catalytic activity, selectivity for C H and stability than
2. The 3D hierarchical structure enhances selectivity. To
further verify the importance of the 3D hierarchical structure,
we performed the CO reduction using the Cu/PANI-CP (I)
2
electrodes prepared at different electrodeposition times. It
shows that the main product over PANI-CP was H , no C H
2
2
4
product was detected (Figure S30A), indicating that PANI is
not active for the reaction. As the amount of Cu increases
(Figure S29), the FE increased with electrodeposition time at
beginning, and then decreased slightly (Figure S30). The main
reason is that the thickness of the Cu 3D layer increases with
increasing electrodeposition time, and thus intermediates
stayed longer time in the Cu layer, which is favorable to CÀC
2
4
other catalysts.
Considering all of observations above, we conclude that
the 3D hierarchical structure obtained by in situ synthetic
strategy is critical to enhance activity, selectivity and stability.
These are further discussed below:
coupling. However, as the Cu layer was too thick, agglomer-
ation of Cu nanosheets occurred and the pores were blocked,
1
. The in situ synthetic strategy creates a favorable micro-
inhibiting diffusion of CO and electrolyte into the layer, and
2
environment to promote activity. First, in situ synthetic
strategy is conducive to the generation of 3D hierarchical
structure, which results in large ECSA (Figure 3A) and
abundant defects (Figure 2) that enhance the activity. Second,
Cu/PANI and PANI/CP contacted very well in the Cu/PANI-
CP (I) electrode because it was fabricated by in situ electro-
deposition. This structure can reduce or eliminated the
interfacial contacting resistance between the components in
the electrode, which is favorable to decrease the onset
potential and applied potential (Figure S8, Figures S12–
S15). In contrast, for Cu/PANI-CP (II, III), the synthesized
Cu NPs are embedded in the polymer. The physical contact
between Cu NPs and the polymer surface result in a tunneling
barrier for electron transfer to the active sites. To elucidate
this point, we use electrochemical impedance spectroscopy
thus the FE of C H reduced with the electrodeposition time.
2
4
3. High dispersion of metal nanosheets improves stability.
In the 3D hierarchical structure, Cu nanosheets are highly
dispersed on 3D polymer, which prevents agglomeration, and
thus Cu/PANI-CP (I) exhibited remarkable stability in
CO RR. This can be known from the fact that the FE and
2
current density of Cu/PANI-CP (I) did not change obviously
with time (Figure 3C, Figure S17).
The above findings are also applicable to the preparation
of other metal based M/PANI-CP (I) (M = Pd, Zn, Sn)
catalysts. The morphology and size of the electrodeposited
samples can be viewed from SEM images (Figure S31). It is
shown that the metals of 3D morphology in the M/PANI-CP
(I) were uniformly deposited on the 3D skeleton of PANI on
the CP. Moreover, the morphologies of these M/PANI hybrids
were significantly different from that of metals NPs deposited
directly onto CP (M-CP (IV)). The XRD and XPS results also
confirmed the successful formation of M/PANI-CP (I) (M =
Pd, Zn, Sn) catalysts (Figure S32). The electrocatalytic
[
18]
(
EIS) to study the interfacial properties of the Cu/PANI-CP
electrodes at an open-circuit potential (OCP; Figure S23) and
CO2 equilibrium potential (Figure 4A,B). Two types of
equivalent circuit was applied to fit the high and medium
1
ꢀ 2021 Wiley-VCH GmbH
Angew. Chem. Int. Ed. 2021, 60, 10977 – 10982