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Chlorobenzene oxidation using ozone over iron oxide and manganese oxide catalysts
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dJournal of Hazardous Materials 186 (2011) 1781–1787
Contents lists available at ScienceDirect
Journal of Hazardous Materials
journa l homepage: www.e lsev ier .com/ locate / jhazmat
hlorobenzene oxidation using ozone over iron oxide and manganese
xide catalysts
ou Chuan Wang, Hsu Shang Liang, Moo Been Chang ?
raduate Institute of Environmental Engineering, National Central University, Chung-Li, Taoyuan County 320, Taiwan
r t i c l e i n f o
rticle history:
eceived 11 October 2010
eceived in revised form
1 December 2010
ccepted 15 December 2010
vailable online 22 December 2010
a b s t r a c t
A low-temperature catalytic oxidation of chlorobenzene (CB) has been performed at temperatures of
60–210 ?C using ozone (O3) over iron oxide and manganese oxide, respectively. In the absence of ozone,
CB conversion achievedwith these two catalysts at 200 ?Cwas below10%.However, addition of 1200ppm
ozone results in a remarkable increase in CB conversion and the conversion reaches 91.7% at 150 ?C for
iron oxide, while 81.5% conversion is achieved with manganese oxide at 90 ?C. The activation energy of
?1 ?1eywords:
ron oxide
anganese oxide
zone
manganese oxide (48kJmol ) is higher than that of iron oxide (43kJmol ) without ozone. However, as
ozone is added, the activation energy is significantly reduced to 20.0 kJmol?1 for iron oxide. CO and CO2
are the only carbon-containing products detected in the effluent gas stream. For the long-term test, no
obvious deactivation was found in iron oxide and ozone. However, in the case of manganese oxide and
ozone, 3% reduction of CB conversion was observed. Slight deactivation might be attributed to a small
duct
catalyhlorobenzene
ow-temperature oxidation
amount of reaction bypro
on the active sites of the
. Introduction
Incinerationhas becomeoneof themainstream technologies for
aste treatment in Taiwan. However, significant amount of chlori-
atedvolatile organic c
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