86
R. Chen et al.
Table 3.2
(continued)
Metal oxide catalyst
Precursor
Deposition temperature
Support
Catalytic reaction
TiO
2
[79, 86, 93, 97–107]
TTIP-H
2 O
[79, 86, 99–101, 103, 104,
107]
TiCl
4 –H
2 O [98, 102, 105]
TDMAT-H
2 O [93, 97]
110 °C [102]
120 °C [97]
150 °C [98–101, 104, 105]
160°C [79]
180 °C [103]
200°C [86, 93, 107]
Cu–chromite [86]
TiO
2 [98, 99, 106]
Al
2 O
3 [100, 101]
Au [102]
Ni [103, 104]
C [105]
ZnO [93]
CNCs [79]
SrTiO
3 [107]
In
2 O
5 Sn [97]
The selective hydrogenation
of furfural [86, 98]
Semihydrogenation of alkyne
to olefin [99]
CO oxidation [100–102]
Carbon dioxide reforming of
methane [103, 104]
Electrochemical water
oxidation [105]
Photo-induced degradation
efficiency of the CSHJ [93]
Nitrobenzene hydrogenation
[79]
1-propanol reforming [106]
Acrolein hydrogenation
selectivity [107]
Solar-driven hydrogen
evolution [97]
(continued)
R. Chen et al.
Table 3.2
(continued)
Metal oxide catalyst
Precursor
Deposition temperature
Support
Catalytic reaction
TiO
2
[79, 86, 93, 97–107]
TTIP-H
2 O
[79, 86, 99–101, 103, 104,
107]
TiCl
4 –H
2 O [98, 102, 105]
TDMAT-H
2 O [93, 97]
110 °C [102]
120 °C [97]
150 °C [98–101, 104, 105]
160°C [79]
180 °C [103]
200°C [86, 93, 107]
Cu–chromite [86]
TiO
2 [98, 99, 106]
Al
2 O
3 [100, 101]
Au [102]
Ni [103, 104]
C [105]
ZnO [93]
CNCs [79]
SrTiO
3 [107]
In
2 O
5 Sn [97]
The selective hydrogenation
of furfural [86, 98]
Semihydrogenation of alkyne
to olefin [99]
CO oxidation [100–102]
Carbon dioxide reforming of
methane [103, 104]
Electrochemical water
oxidation [105]
Photo-induced degradation
efficiency of the CSHJ [93]
Nitrobenzene hydrogenation
[79]
1-propanol reforming [106]
Acrolein hydrogenation
selectivity [107]
Solar-driven hydrogen
evolution [97]
(continued)