Angewandte
Communications
Chemie
(< 8 mmolhꢀ1). The production rate of KA oil increased with
the applied bias and became saturated at cell voltages above
1.5 V. The generation rate of KA oil then reached
41.2 mmolhꢀ1 at a cell voltage of 2.0 V, although KA oil was
scarcely observed below 2.0 V in the dark. It should be noted
that no oxidation products derived from cyclohexane were
obtained by the conventional electrochemical oxidation
system in the dark using either the Pt, glassy carbon, or
graphite electrodes, even when the anodic current was
observed at high anodic potential. These results indicate
that the selective oxidation of cyclohexane to KA oil was
performed on a WO3 photoanode at a low cell voltage using
simulated solar-light assistance.
The presence of O2 is important for KA oil production on
the photoanode as well as for O2 reduction on the Pt CE. The
oxidative transformation of cyclohexane to KA oil generally
required O2. It was reported that the selectivity for producing
KA oil decreased with the O2 concentration, and bicyclohexyl
was mainly formed at low oxygen concentrations by thermal
catalytic reactions over solid supported CuII, FeIII, CrIII, and
CoIII salts.[2] The reaction mechanism shown in Equation (1)
Figure 5. Reaction time dependence of the accumulation of cyclohex-
anol (diamonds), cyclohexanone (circles), and the mole ratio of
cyclohexanone/cyclohexanol (open squares) using a WO3 electrode
under an O2 (a) and N2 (b) atmosphere with simulated solar-light
irradiation (100 mWcmꢀ2). Composition of the electrolyte: 18 mL
cyclohexane, 12 mL tBuOH, and 2 mL HNO3; working electrode: WO3
electrode (2ꢀ2 cm2); counter electrode: Pt mesh. Electrolysis was
conducted in constant potential mode at 0.5 V vs. counter electrode.
Partial oxidation selectivity ¼
½ðC-ol þ C-oneÞ=ðC-ol þ C-one þ ð1=6Þ CO2Þꢁ 100
ð2Þ
Evaluation of the faradaic efficiency of this reaction is
difficult when the reaction mechanism is not clear, because
there is a possibility that reaction of a radical intermediate
with O2 will take place through chain reactions. The apparent
faradaic efficiency was defined as the current utilization ratio
of KA oil to the charge passed [Eq. (3); see the Supporting
was proposed.[10] The oxidation of cyclohexane proceeds via
a cyclohexyl radical by a single-electron transfer process, and
it reacts with O2 to form the cyclohexylperoxyl radical.
Bicyclohexyl was often detected by coupling of a cyclohexyl
radical when O2 was absent. Subsequently, the generated pair
of cyclohexyperoxyl radicals are disproportionated to form
the same amount of C-ol and C-one. C-ol possibly underwent
an additional two-electron oxidation to C-one.
Figure 5 shows the time dependence of C-ol and C-one
production by oxidation of cyclohexane on a WO3 photo-
anode under O2 and N2 atmospheres with simulated solar-
light irradiation. Under an N2 atmosphere, a negligible
amount of KA oil was detected and a small amount of
bicyclohexyl (10.6 mmol) was formed, although the photo-
current was almost identical to that under the O2 atmosphere.
In the presence of O2, both C-ol and C-one were produced
effectively. The ratio of produced C-one to C-ol increased
with the reaction time. We confirmed that C-ol was oxidized
to C-one in the tBuOH/HNO3 electrolyte (without cyclohex-
ane) on the WO3 photoanode, suggesting that excess C-one is
obtained by the oxidation of produced C-ol [Eq. (1)].
Current utilization ratio of KA oil ðapparent faradaic efficiencyÞ ¼
½ð3C-oneꢀC-olÞ=ðCharge passed=96485Þꢁ 100
ð3Þ
Information], and this was calculated as appproximately
76%. All these results indicate that the hole in the valence
band of WO3 selectively oxidized the cyclohexane to KA oil,
while the solvent might be partially oxidized. The prepared
WO3 photoanode was suitable and was reused at least five
times without necessitating a regeneration process. A turn-
over number (moles of cylohexanol and cyclohexanone per
moles of WO3) of 57 was obtained.
Finally, the incident photon to current efficiency (IPCE,
the apparent quantum efficiency to photocurrent) of this
photoanode reaction method was measured under mono-
chromatic light using a band pass filter (Figure 6, diamonds).
The IPCE spectrum was similar to the absorption spectrum of
the WO3 photoelectrode in the visible-light region (see
Figure S5). The IPCE at 400 and 420 nm were 40% and
24%, respectively. The maximum IPCE of 57% was obtained
at a wavelength of 365 nm. These high values indicate the
advantages of the efficient photo-electrochemical reaction for
KA oil production. The IPCE in the shorter wavelength
region at less than 365 nm was low mainly because of the
absorption of the electrolyte solution (see Figure S6). For
comparison, the IPCE spectrum in 1.0m aqueous HClO4
without any organic substrate for O2 evolution from H2O is
The production of CO2 gas was reported by the complete
oxidation of cyclohexane with O2.[3,4,11] Under our experi-
mental conditions (charge passed: 21 C, cell voltage: 0.5 V,
reaction time: 5 h), the amount of CO2 produced was small
(7 mmol) compared with that of C-ol (34 mmol) and C-one
(67 mmol). The partial oxidation selectivity, which is defined
by Equation (2),[3e,5,12] was 99%. This value is high compared
with that for the photocatalytic reaction on Pt-WO3 (93%).[5]
Angew. Chem. Int. Ed. 2018, 57, 1 – 5
ꢀ 2018 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
3
These are not the final page numbers!