Entrya | Substrate | Content of H2O2 (mmol) | Initial reaction rateb (mmol/L/h) | Conversion (%)c | yield (%)c |
---|---|---|---|---|---|
1 | 1 | 93.99 ± 6.41 | 57.21 ± 0.82 | 49.17 ± 1.22 | |
2 | 2.5 | 121.87 ± 9.26 | 91.99 ± 0.04 | 74.5 ± 1.99 | |
3 | 5 | 176.15 ± 1.78 | 99.89 ± 0.08 | 91.37 ± 1.94 | |
4 | 7.5 | 232.88 ± 1.76 | 99.65 ± 0.07 | 92.04 ± 3.08 | |
5 | 10 | 239.81 ± 5.23 | 99.73 ± 0.11 | 86.75 ± 0.24 | |
6 | 15 | – | 74.53 ± 5.6 | 67.96 ± 8.45 | |
7 | 30 | – | 20.56 ± 7.12 | 12.8 ± 1.99 | |
8 | 45 | – | 6.37 ± 5.28 | 6.25 ± 0.89 | |
9 | 1 | 4.22 ± 0.09 | 22.17 ± 0.35 | 8.13 ± 0.54 | |
10 | 2.5 | 4.35 ± 0.91 | 49.15 ± 0.36 | 36.68 ± 1.97 | |
11 | 5 | 5.29 ± 0.05 | 62.11 ± 0.33 | 45.77 ± 2.3 | |
12 | 7.5 | 5.79 ± 0.19 | 66.44 ± 0.91 | 56.24 ± 3.95 | |
13 | 10 | 6.34 ± 2.35 | 63.95 ± 1.41 | 56.3 ± 0.59 | |
14 | 1 | 6.31 ± 0.3 | 15.91 ± 0.88 | 14.25 ± 2.1 | |
15 | 2.5 | 6.62 ± 1.18 | 68.82 ± 0.42 | 50.02 ± 3.94 | |
16 | 5 | 9.23 ± 2.65 | 83.53 ± 0.42 | 65.35 ± 4.49 | |
17 | 7.5 | 9.59 ± 0.19 | 89.02 ± 0.64 | 76.56 ± 1.22 | |
18 | 10 | 9.72 ± 1.39 | 84.79 ± 1.15 | 70.38 ± 1.69 |