from coal-fired flue gas. The catalyst with ordered pore structure can lower mass transfer resistance resulting in higher Hg
0
oxidation efficiency. Therefore
in the present work
wood vessels were used as sacrificial template to obtain Co
3
O
4
with ordered pore structure. SEM and BET results show that
when the mass concentrations of Co(NO
3
)
2
·6H
2
O was 20%
the obtained catalyst (Co
3
O
4
[20%Co(NO
3
)
2
]
) possesses better pore structure and higher surface area. It will expose more available surface active sites and lower the mass transfer resistance. Furthermore
XPS results prove that Co
3
O
4
[20%Co(NO
3
)
2
]
has the highest ratio of chemisorbed oxygen which plays an important role in Hg
0
oxidation process. These results lead to a better Hg
0
oxidation efficiency of Co
3
O
4
[20%Co(NO
3
)
2
]
which is about 90% in the temperature range of 200 to 350 ℃. Furthermor
e
Co
3
O
4
[20%Co(NO
3
)
2
]
has a stable catalytic activity
and its Hg
0
oxidation efficiency maintains above 90% at 250 ℃ even after 90 h test. A probable reaction mechanism is deduced by the XPS results of the fresh
used and regenerated catalyst of Co
3
O
4
[20%Co(NO
3
)
2
]
. Chemisorbed oxygen can react with Hg
0
forming HgO with the reduction of Co
3+
to Co
2+
. And lattice oxygen and gaseous oxygen can supplement the consumption of chemisorbed oxygen to oxidize Co
2+
to Co
3+
.
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