134
6 Conversion of Methane to Aromatic Hydrocarbons
Table 6.2
Catalytic performance of Mo species supported on various supports in a fixed-bed continuous-flow reactor
Catalyst
Mo/wt% CH
4
conversion/%
Selectivity/C-atom%
Reaction
temperature/K
Time on
stream/h
Ref.
Benzene Toluene Naphthalene C
2
hydrocarbons
Coke
Mo/Al
2 O
3
3
7.4
3.9
0.1
0
2.1
88.9
973
40
[21]
Mo/SiO
2
3
5.3
8.7
0.4
0.3
2.1
86.6
973
40
[21]
MoO
3
–
0.01
0
0
No data
100
44
973
110
[25]
6 Conversion of Methane to Aromatic Hydrocarbons
Table 6.2
Catalytic performance of Mo species supported on various supports in a fixed-bed continuous-flow reactor
Catalyst
Mo/wt% CH
4
conversion/%
Selectivity/C-atom%
Reaction
temperature/K
Time on
stream/h
Ref.
Benzene Toluene Naphthalene C
2
hydrocarbons
Coke
Mo/Al
2 O
3
3
7.4
3.9
0.1
0
2.1
88.9
973
40
[21]
Mo/SiO
2
3
5.3
8.7
0.4
0.3
2.1
86.6
973
40
[21]
MoO
3
–
0.01
0
0
No data
100
44
973
110
[25]