Table 1.
H2 production by various catalysts from FA degradation reaction.
| Entry | Catalyst | H2 produced (mmol) | TOF under Vis | |
|---|---|---|---|---|
| Under Vis | Dark room | |||
| 1 | TiO2 | – | – | – |
| 2 | GO | – | – | – |
| 3 | NiPc | 0.61 | 0.067 | 34 |
| 4 | TiO2/NiPc | 0.63 | 0.067 | 35 |
| 5 | TiO2/GO | 0.49 | – | – |
| 6 | NiPc@GO | 0.92 | 0.045 | 51 |
| 7 | TiO2 (0.03 g)/NiPc (18 µmol)@GO | 1.34 | 0.054 | 74 |
| 8 | TiO2 (0.04 g)/NiPc (18 µmol)@GO | 1.38 | 0.054 | 77 |
| 9 | TiO2 (0.05 g)/NiPc (18 µmol)@GO | 1.38 | 0.054 | 77 |
| 10 | TiO2 (0.04 g)/NiPc (12 µmol)@GO | 0.98 | 0.052 | 81 |
| 11 | TiO2 (0.04 g)/NiPc (24 µmol)@GO | 1.59 | 0.057 | 66 |
| 12 | TiO2 (0.04 g)/NiPc (30 µmol)@GO | 1.68 | 0.058 | 56 |
Reaction conditions: FA (30 ml), catalyst, r.t., 1 h.