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indicates that HCHO is more easily oxidized over these samples
at high temperature. The HCHO conversion efficiency of the
TiO2/CeO2 nanowires is much higher than the pristine TiO2
nanowires and CeO2 nanowires in the entire temperature
windows, conrming the superior catalytic activity of the TiO2/
CeO2 nanowires. Second, at a low temperature of 20 ꢀC,
approximately 20% of HCHO could be converted over the TiO2/
CeO2 nanowires, while only 3% and 4% for pristine TiO2
nanowires and CeO2 nanowires, respectively. Third, with the
Fig. 3 (a) H2-TPR profiles of the TiO2 nanowires, CeO2 nanowires and
TiO2/CeO2 nanowires. (b) CV curves of the TiO2 nanowires, CeO2
nanowires and TiO2/CeO2 nanowires obtained at a scan rate of 100
ꢀ
reaction temperature increased to 60 C, the TiO2/CeO2 nano-
wires yielded a remarkably higher HCHO conversion efficiency
of 60.2%, whereas the TiO2 and CeO2 nanowires only achieved
9.5% and 18.8%, respectively, at the same temperature. More-
over, such low reaction temperature for 60% HCHO conversion
obtained for TiO2/CeO2 nanowires is substantially lower than
the values recently reported for most of non-precious cata-
lysts24–27 and some precious catalysts,14,17 such as 3D-Co3O4 (110
ꢀC),24 and MnO2/cellulose (120 ꢀC),27 MnOx–CeO2 (80 ꢀC),25
MnxCo3ꢁxO4 (65 ꢀC),26 Au/CeO2 (70 ꢀC),17 1% Rh/TiO2 (75 ꢀC).14
Fig. 2b compares the HCHO conversion efficiencies of our TiO2/
CeO2 nanowires with other reported catalysts at low tempera-
ture ranging from 20 to 80 ꢀC. Signicantly, the HCHO
conversion performances of the TiO2/CeO2 nanowires at low
temperatures are substantially higher than most reported no-
precious catalysts, and even comparable to the previously
reported precious catalysts, such as Au/CeO2 17,21 and Ag/MnOx–
CeO2.20 All the above results fully validate that the TiO2/CeO2
nanowires possess signicantly high catalytic activity for HCHO
oxidation at low temperature.
mV sꢁ1
.
ꢀ
CeO2, while the high-temperature reduction peak at 708 C is
ascribed to the lattice oxygen of CeO2.28 Reduction of TiO2 alone
is more difficult and essentially no TPR peak was observed from
30 to 750 ꢀC. Importantly, signicant enhancement in the
reducibility was observed for the TiO2/CeO2 composite sample.
A new reduction peak (marked by green dash rectangle)
occurred in the range from 200 to 350 ꢀC, which is attributed to
the synergistic effect of CeO2 and TiO2 nanowires. This reduc-
tion peak makes the major contribution to HCHO oxidation in
comparison with the other two reduction peaks in the high
ꢀ
ꢀ
temperature region around 560 C and 708 C. In general, the
lower temperature of the corresponding desorption peak
ꢀ
centered at the 200–350 C range indicates that it is easier to
generate surface active oxygen species, which may offer a higher
catalytic activity in oxidation reactions. The lowering of reduc-
tion temperature implies that the presence of CeO2 helps to
weaken the surface oxygen on TiO2/CeO2 nanowires, and
therefore improves the reducibility of the catalyst.
Beside the conversion efficiency, the long-term stability of
the catalyst is also very important for their practical applica-
tions. To evaluate the catalytic stability of the TiO2/CeO2
nanowires, the catalytic oxidation performance of HCHO over
Cyclic voltammogram (CV) curves of the pristine TiO2
nanowires, CeO2 nanowires and TiO2/CeO2 nanowires collected
at a scan rate of 100 mV sꢁ1 in HCHO (40%) aqueous electrolyte
are displayed in Fig. 3b. All the samples showed approximately
rectangle-like shapes, revealing the electric double layer
capacitance characteristic. The substantially higher current
density of the TiO2/CeO2 sample over the pristine TiO2 and
CeO2 samples show that it possesses larger surface area. The
specic surface area of the pristine TiO2, CeO2, and TiO2/CeO2
samples is about 18.3, 24.4 and 36.7 m2 gꢁ1, respectively. Given
the experimental results above, two possible reasons are
proposed to explain the signicantly enhanced catalytic
performance of the TiO2/CeO2 nanowires. First, a good inter-
facial contact between CeO2 and TiO2 nanowires would form
legitimately, which could allow HCHO to be absorbed easily. In
addition, CeO2 is rich in oxygen vacancy defects and has a large
oxygen storage capacity, which is benecial for the HCHO
catalytic oxidation. Second, the free-standing 1D nanowires
grown on carbon cloth not only offer a large surface area for
surface reactions, but also enable the fast transport of species
and extend the reaction sites from the surface to the subsurface
of the catalysts. In order to study the optimizational ratio of the
CeO2 on the TiO2 nanowires, we deposited CeO2 on the TiO2
nanowires at different durations and studied their catalytic
performance, which are shown in Fig. S6.† Signicantly,
ꢀ
TiO2/CeO2 nanowires on stream at 60 C for 100 h is shown in
Fig. 2c. Impressively, the TiO2/CeO2 nanowires exhibited a
remarkable long-term catalytic stability with only less than 3%
decrease in HCHO conversion efficiency aer 100 h. Fig. S5a†
displays the TG curve of TiO2/CeO2 nanowires performed in air
ow from 35 to 900 ꢀC. Less than 2% of mass loss was observed
for the TiO2/CeO2 nanowires below 600 ꢀC, indicating the
excellent thermal stability of TiO2/CeO2 nanowires between 35
ꢀ
to 600 C. SEM observations reveal that the morphology of the
TiO2/CeO2 nanowires was preserved aer 100 h long-test
(Fig. S5b†). Additionally, XRD (Fig. S5c†) and XPS (Fig. S5d†)
survey spectra conrm that there were no obvious changes in
the phase and chemical composition of TiO2/CeO2 nanowires
aer testing for 100 h. Thus, the remarkable stability of the
TiO2/CeO2 nanowires is due to their excellent thermal strength,
morphology and phase stability as well as exible free-standing
carbon cloth, which could offer high mechanical stability.
To gain insights into the reasons for the excellent catalytic
performance of TiO2/CeO2 nanowires, the H2-temperature-
programmed reduction (TPR) analysis was carried out. Fig. 3a
compares the H2-TPR proles of the TiO2, CeO2 and TiO2/CeO2
samples. The pristine CeO2 nanowires exhibited two reduction
peaks, and the low-temperature reduction peak located at 485
ꢀC is attributed to the reduction of surface capping oxygen of
This journal is © The Royal Society of Chemistry 2015
RSC Adv., 2015, 5, 7729–7733 | 7731