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H2O molecules in the structure of 1–3 all bind in an anti
fashion with respect to the diiron vector. In particular, the
difference in ligand flexibility and coordination geometry
among 1–3 provides a research platform for understanding
the relationship between structure and catalytic activity and
exploring the details of mechanism.
different scan rates, the peak currents varied linearly with the
square root of the scan rate (Figure S9a), which indicates
a diffusion-controlled process. This is assigned as the one-
electron reduction of Fe2(III,III) to Fe2(III,II). After two
irreversible oxidative processes, the CV of 0.5 mM complex
1 exhibited a significant catalytic activity, during the scanning
at 100 mVsꢀ1 from 0.24 to 2.0 V vs. NHE (Figure 2a, Fig-
ure S10). CVs were further recorded at different scan rates
and the resulting normalized catalytic currents increased with
decreasing scan rate (Figure S9b), consistent with a water
oxidation catalysis process. The onset potential for water
oxidation appears at 1.57 V vs. NHE with an overpotential of
ꢁ 830 mV followed by two oxidative waves. When complex 2
was used as WOC under the same condition, only one
irreversible catalytic process was observed at 1.76 V vs. NHE
(Figure 2b, Figures S11 and S12b) and the catalytic current is
lower than 1. Complex 3 displays two oxidative waves at 1.36
and 1.64 V vs. NHE (Figure 2c, Figure S13), but normalized
catalytic currents of 3 nearly keep constant at different scan
rates (Figure S14), indicating that complex 3 cannot catalyze
water oxidation. Additionally, simple Fe3+ ion catalyzed water
oxidation was excluded by control experiments. 1.0 mM of
Fe(NO3)3, Fe(ClO4)3 and FeCl3 were examined under iden-
tical conditions, respectively (Figure S15). All Fe3+ ions
showed no activity towards water oxidation indicating that
the observed catalytic activity is not caused by free Fe3+ ions
or formed iron oxides which may possibly exist during
catalysis.
The oxygen evolution was further confirmed by con-
trolled-potential electrolysis (CPE) (Figure 3a) using a 2 cm2
BDD disk working electrode. For CPE at 1.57 V vs. NHE,
complex 1 exhibits the highest catalytic current density of
0.7 mAcmꢀ2, followed by complex 2 with 0.3 mAcmꢀ2 and
complex 3 shows negligible 30 mAcmꢀ2 equivalent to blank
current. The dissolved oxygen was also measured by a cali-
brated Ocean Optics FOXY probe during CPE (Figure 3b).
The concentration of O2 dissolved in the solution phase
increased from 54 mM to 301 mM for 1, from 54 mM to 180 mM
for 2 and negligible for 3. For both 1 and 2, the Faraday
efficiency for the O2 evolution is above 90% in initial 5
minutes (Table S1). The oxygen evolution rate for 1 is about 2
times faster than 2, and 3 is inactive toward catalytic water
oxidation, indicating that the catalytic activity is strongly
dependent on the choice of ligand and the regulation of the
ligand framework can achieve tuning its catalytic perfor-
mance.
We firstly determined the pKa values of the aqua ligand of
1–3 [Eq. (1)–(2)] by potentiometric titration. The pKa1 values
are 4.41, 4.93 and 4.96 for 1H O=H O, 2H O=H O and 3H O=H O
,
2
2
2
2
2
2
respectively. The pKa2 values are 5.22, 5.81 and 6.10 for
H O=HO, 2H O=HO and 3H O=HO, respectively (Figures S4–S6 and
1
2
2
2
Table S2). It can be found that as the rigidity of the ligand
increases, the acidity of the aqua ligand gradually decreases.
To a certain extent, this indicates that the chemical reactivity
of the aqua ligand is sensitive to the regulation of the ligand.
According to the pKa2 values, the HO-FeIII-O-FeIII-OH
species is the dominant existence at pH > 8 buffer solution
(Figures S4–S6). In terms of acetate,[19] phosphate[20] and
sulphate[10b,20] could play as bridge ligand to inhibit the
catalytic efficiency by occupying the coordination sites of
water molecules, diiron(III) complexes in 0.1 M NaHCO3
(pH 8.4) solution was applied for electrocatalytic water
oxidation investigation.[21]
Electrochemical behavior and oxygen evolution of diiron
complexes 1–3. Figure 2 shows the CVs of 0.5 mM complex 1–
3 in 0.1 M NaHCO3 (pH 8.4) using BDD electrode. For
complex 1, on the cathodic direction, an irreversible cathodic
process at Epc = ꢀ0.23 V vs. NHE was observed in the CV, and
an irreversible anodic process at Epa = 0.40 V vs. NHE was
observed in the reverse scan (Figure S8, with peak–peak
splitting DEp = 630 mV). When the CV was measured at
The stability of 1 and 2 during the electrocatalytic process
was further examined by electrode analysis after long time
bulk electrolysis (Figure S16). The morphology of electrode
did not change before and after electrolysis in scanning
electron microscopy (SEM) images (Figure S17), which
indicated that there was no FexOy formation during the
electrocatalytic process. Moreover, X-ray photoelectron
spectroscopy (XPS, Figure S18) analysis indicated that no
Fe species such as FexOy were deposited on the electrode
surface, and rinse tests also showed that there was no active
species attached to the electrode surface (Figure S19). CVand
UV-vis absorption of the solution after electrolysis was
consistent with the fresh solution (Figures S20–S22), indicat-
Figure 2. CVs recorded in 0.1 M NaHCO3 (pH 8.4) solution using
a BDD electrode without (black line) and with 0.5 mM 1 ((a) red line),
0.5 mM 2 ((b) blue line), and 0.5 mM 3 ((c) green line); the scan rate
was 100 mVsꢀ1
.
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ꢀ 2021 Wiley-VCH GmbH
Angew. Chem. Int. Ed. 2021, 60, 2 – 10
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