Table 1 Optimization conditions of Fe3O4@void@C-Schiff-base/Pd catalyst amount, solvent, and temperature on model reaction.
Entry | Solvent | Base | Cat (g) | T(°C) | t [min] | Yield [%]a |
|---|---|---|---|---|---|---|
1 | H2O | K2CO3 | – | 60 oil bath | 540 | – |
2 | H2O | K2CO3 | 0.001 | 60 | 90 | 90% |
3 | H2O | K2CO3 | 0.003 | 60 | 60 | 95% |
4 | H2O | K2CO3 | 0.005 | 60 | 50 | 98% |
5 | H2O | K2CO3 | 0.01 | 60 | 50 | 98% |
6 | H2O | K2CO3 | 0.005 | rt | 360 | Trace |
7 | H2O | K2CO3 | 0.005 | 40 | 240 | 58% |
8 | H2O | K2CO3 | 0.005 | 50 | 180 | 70% |
9 | H2O | K2CO3 | 0.005 | 80 | 50 | 98% |
10 | H2O | Na2CO3 | 0.005 | 60 | 60 | 76% |
11 | H2O | NEt3 | 0.005 | 60 | 60 | 58% |
12 | H2O | NaOH | 0.005 | 60 | 60 | 43% |
13 | H2O | Free base | 0.005 | 60 | 60 | Trace |
14 | EtOH | K2CO3 | 0.005 | 60 | 60 | 93% |
15 | EtOH/H2O | K2CO3 | 0.005 | 60 | 60 | 97% |
16 | Toluene | K2CO3 | 0.005 | 60 | 60 | 50% |
17 | DMSO | K2CO3 | 0.005 | 60 | 60 | 58% |
18 | DMF | K2CO3 | 0.005 | 60 | 60 | 55% |
19 | CCl4 | K2CO3 | 0.005 | 60 | 60 | 43% |
20b | H2O | K2CO3 | 0.005 | 60 | 60 | 50 |
21c | H2O | K2CO3 | 0.005 | 60 | 60 | – |
22d | H2O | K2CO3 | 0.005 | 60 | 60 | – |
