640
Fig. 6 Various products obtained during the oxidation of FUR
Table 5 Summary of oxidation of FUR with different catalysts
Reaction
condition
Reactant Product Catalyst
Performance
Refs.
Conversion
(%)
Yield
(%)
593 K, 5.7 kPa O 2 FUR
MAN VO x /Al 2 O 3
100
73
[5]
383 K, 14 h,
20 atm O 2
FUR
MAN H 5 PV 2 Mo 10 O 40 and
Cu(CF 3 SO 3 ) 2
98.7
54
[95]
633 K, 21% O 2 /N 2
atm
FUR
MAN VPO HT
100
90
[96]
573 K, 1.68 kPa
O 2
FUR
MAN V 2 O 5 /γ-Al 2 O 3
100
55
[97]
343 K, 1 h
FUR
MA
VZPK1 (0.25 Zr/V ratio
loading)
81.2
29.2
[98]
373 K, 4 h
FUR
MA
TS-1 and acetic acid
100
62
[100]
403 K, 4 h,
0.275 MPa O 2
HMF
DFF
Ru/γ-Al 2 O 3
99
96
[101]
383 K, 2.0 MPa
O 2
HMF
DFF
Ru/C
100
96
[102]
383 K, 4 h,
2.0 MPa O 2
HMF
DFF
Ru/OMC-P0.56
100
88
[103]
383 K, 2 h,
1.0 MPa O 2
HMF
DFF
Ru 1 /NiO
91.1
74
[104]
413 K, 6 h, in air HMF
DFF
NH 4 ·V 3 O 8 /Fe 3 O 4
95.5
79.1
[105]
353 K, 5 h, TBHP HMF
DFF
Co x O y -N@TiO 2
91
36.4
[106]
413 K, 2 h, 3 MPa
air
HMF
DFF
Mn 0.50 -Co 0.50 -O
42.6
41.7
[107]
343 K, 8 h,
0.4 MPa O 2
HMF
DFF
Cu/NG 4 , TEMPO
99.8
99.2
[108]
363 K, 1 h,
0.8 MPa O 2
HMF
DFF
MnO x microtubes
50.4
50.4
[109]
383 K, 10 h,
0.2 MPa O 2
HMF
DFF
MgO·MnO 2 ·CeO 2
98.8
94
[110]
373 K, 15 h,
0.9 MPa O 2
HMF
DFF
MgO·CeO 2
97.8
95.8
[111]
373 K, 12 h,
1 MPa O 2
HMF
DFF
Cs/MnO x
98.4
94.7
[112]
393 K, 7 h, in air HMF
DFF
10V 2 O 5 @Cu−MOR(125) >99.9
91.5
[113]
373 K, 6 h, 1 MPa
O 2
HMF
DFF
FeCo/C(500)
100
>99
[114]
M. Baithy et al.