Table 1 Optimization of the reaction conditionsa
Entry | Catalyst | Solvent | T (°C) | 3a | 3a | 4a | 4a |
|---|---|---|---|---|---|---|---|
Yield (%)b | d.r.c | Yield (%)b | d.r.c | ||||
1 | MgI2 | THF | 25 | 17 | 7:1 | <5 | – |
2 | ZnCl2 | THF | 25 | 23 | 2:1 | 0 | – |
3 | CuI | THF | 25 | 80 | 3:1 | 0 | – |
4 | CuBr | THF | 25 | 78 | 4:1 | <5 | – |
5 | CuCl | THF | 25 | 95 | 16:1 | 0 | – |
6 | Cu(CH3CN)4PF6 | THF | 25 | 92 | 6:1 | 0 | – |
7 | Cu(OAc)2 | THF | 25 | 81 | 3:1 | 0 | – |
8 | CuF2 | THF | 25 | 38 | 1:1 | 10 | 2:1 |
9 | CuCl2 | THF | 25 | 49 | 5:1 | 38 | 6:1 |
10 | CuBr2 | THF | 25 | 17 | 2:1 | 44 | 7:1 |
11 | CuCl | toluene | 25 | 90 | 18:1 | 0 | – |
12 | CuCl | CH2Cl2 | 25 | 97 | 6:1 | 0 | – |
13 | CuCl | MeOH | 25 | 50 | 15:1 | 0 | – |
14 | CuCl | THF | 25 | 93 | 12:1 | 0 | –d |
15 | CuCl | THF | 60 | 97 | >20:1 | 0 | – |
16 | – | THF | 25 | 0 | – | 0 | – |
17 | – | THF | 60 | 22 | – | 0 | –e |
18 | CuBr2 | toluene | 25 | 9 | 4:1 | 33 | 3:1 |
19 | CuBr2 | CH2Cl2 | 25 | 12 | 2:1 | 15 | 2:1 |
20 | CuBr2 | DMSO | 25 | 24 | 2:1 | 64 | 3:1 |
21 | CuBr2 | DMA | 25 | 19 | 1:1 | 56 | 4:1 |
22 | CuBr2 | DMF | 25 | 13 | 2:1 | 55 | 12:1 |
23 | CuBr2 | DMF | 25 | 26 | 3:1 | 69 | 6:1f |
24 | CuBr2 | DMF | 25 | 64 | 15:1 | 36 | 9:1g |
25 | CuBr2 | DMF | 25 | 8 | 1:1 | 70 | 9:1 f,h |
26 | CuBr2 | DMF | 60 | 16 | 1:1 | 78 | >20:1f,h |
