Job/Unit: I42152
/KAP1
Date: 06-08-14 18:09:52
Pages: 10
FULL PAPER
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the FeF2 product was calcined at 500 °C for 4 h in air at a heating
rate of 1 °Cmin–1.
Product Characterization: Powder X-ray diffraction (PXRD)
measurements were carried out with a Bruker D8 Advance Powder
X-ray diffractometer with Cu-Kα (λ = 0.154 nm) radiation source
operating at 40 kV and 40 mA. TEM images were taken with a
JEOL-JEM-2010 transmission electron microscope using an
accelerating voltage of 200 kV. The size and morphology of the
product were observed with a field-emission scanning electron mi-
croscopy (FESEM). The porous textures of the prepared materials
were analyzed at 77 K by using a Micromeritics ASAP 2000 sys-
tem. The BET surface areas of the urchin-like α-Fe2O3 nanoarchi-
tectures were measured by the adsorption/desorption isothermal
method, and the pore-size distributions were calculated from the
desorption isotherm by using the BJH model. The surface areas of
the urchin-like FeF2 nanoarchitectures were measured by N2 ad-
sorption with the single-point method. FTIR spectra were recorded
with a Nexus-870 Fourier-transform spectrophotometer in the
range 400–4000 cm–1 using KBr pellets. The X-ray photoelectron
spectroscopy (XPS) measurements were performed with an Axis
Ultra DLD by using Al-Kα radiation. Thermogravimetric analysis
(TGA) was performed with a Perkin–Elmer Diamond thermogravi-
metric analyzer in air from room temperature to 800 °C at a heating
rate of 10 °Cmin–1 and an air flow of 10 mLmin–1.
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Catalytic Reactions: To test the catalytic activity of porous urchin-
like α-Fe2O3 nanoarchitectures, the direct catalytic conversion of
methane was carried out in a quartz tube microreactor (600 mm
length, 8 mm i.d.). The catalyst (0.5 g) was used in all runs. Mass
flow controllers were used to control the flow of CH4 and O2. Flow
rates of CH4 and O2 of 30.0 and 10.0 mLmin–1, respectively, were
typically used. The catalyst was pretreated in an O2 gas flow at
130 °C for 2 h and then purged with high-purity N2 at the same
temperature. The reactant mixture of CH4 and O2 was then
switched to the reactor after the catalyst bed had been heated to
the desired reaction temperature. Products from the reactor outlet
were analyzed with an on-line GC equipped with a TCD detector
and a GDX-502 and carbon sieves (5 Å) column in parallel. The
catalyst activity was evaluated in the temperature range of 110–
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Supporting Information (see footnote on the first page of this arti-
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The authors are grateful for financial support from the National
Natural Science Foundation of China (NSFC) (grant number
21303058), the Shanghai Municipal Natural Science Foundation
(grant number 13ZR1412400), and the key project of the Shanghai
Science and Technology Committee (grant number 11JC1403400).
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