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. 2011 Sep 9;76(21):8781–8793. doi: 10.1021/jo201511d

Table 1. Optimization of the Catalyst System and Choice of PG.

graphic file with name jo-2011-01511d_0006.jpg

entry R cat. oxidant yield (%)
1 Ac (1a) Cu(NO3)2c tBHP 54
2 Ac (1a) CuBr tBHP 47
3 Piv (1b) Cu(NO3)2c tBHP 26
4 Piv (1b) CuBr tBHP 21
5 Bn (1c) Cu(NO3)2c tBHP 60
6 Bn (1c) CuBr tBHP 36
7 Bz (1d) Cu(NO3)2c tBHP 40
8 Bz (1d) CuBr tBHP 10
9 CBz (1e) Cu(NO3)2c tBHP 60
10 CBz (1e) CuBr tBHP 41
11 Tos (1f) Cu(NO3)2c tBHP traces
12 Tos (1f) CuBr tBHP traces
13 2-Py (1g) Cu(NO3)2c tBHP 61
14 2-Py (1g) CuBr tBHP 44
15 Boc (1h) Cu(NO3)2c tBHP 79
16 Boc (1h) CuBr tBHP 72
17 Boc (1h) CuCN tBHP (65)
18 Boc (1h) Cu(OAc)2 tBHP (74)
19 Boc (1h) CuI tBHP (61)
20 Boc (1h) CuBr tBHP (73)
21 Boc (1h) CuCl tBHP (74)
22 Boc (1h) CuF2 tBHP (76)
23 Boc (1h) CuCl   nca
24 Boc (1h) CuCl2   nca
25 Boc (1h) Cu(NO3)2c H2O2 (30%) tracesb
26 Boc (1h) Cu(NO3)2c mCPBA tracesb
27 Boc (1h) Cu(NO3)2c DBPO tracesb
28 Boc (1h)   tBHP nc

nc = no conversion.

a

1 equiv of catalyst was employed.

b

Monitoring according to GC/MS, conversion in parentheses according to HPLC.

c

Cu(NO3)2·3H2O employed.