Table 2.
| ||||
---|---|---|---|---|
Entry | 1 | t [h][b] | 3 | Yield [%][c] |
1 | 1; 5 | 96 | ||
2 | 1; 5 | 93 | ||
3 | 1; 5 | 95 | ||
4 | 1;[d] 5 | 71 | ||
5 | 1;[d] 5 | 70 | ||
6 | 1; 12 | 82 | ||
7 | 1; 12 | 92 | ||
8 | 1; 12 | 95 | ||
9 | 1; 24 | 96 | ||
10 | 1; 5 | 85 | ||
11 | 1; 5 | 90 | ||
12 | 1; 4 | 89 | ||
13 | 1;[e] 24 | 82 | ||
14 | 1; 4 | 91 | ||
15 | 2; 12[f] | 81 | ||
16 | 2; 12[f] | 79 | ||
17 | 2; 12[f] | 91 | ||
18 | 2; 12[f] | 74 | ||
19 | 1; 12 | 75 |
Reactions typically run on 0.2 mmol scale. 1 (2.1 equiv), 2 (1.0 equiv, 0.08 m), Zn(tmp)2 (1.0 equiv).
Reaction time for deprotonation and amination step respectively.
Yield of isolated product.
Zn-(tmp)2·LiCl·MgCl2[4g] was used as base to form stable zincate intermediates.
Deprotonation step run in CH2Cl2 because of the poor solubility of 1m in THF.
Amination step run at 50°C.