Table 1.
Reaction optimization.
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| Entry | Variation from standard conditionsa | % Yieldb |
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| 1 | none | 46 |
| 2 | Pt (+) | C (–) instead of Pt (+) | Pt (–) | ≪25c |
| 3 | C (+) | Pt (–) instead of Pt (+) | Pt (–) | 40 |
| 4 | DMSO as solventd | <22 |
| 5 | MeOH as solventd | n.d.e |
| 6 | Bu4NCl instead of Bu4NBrd | 35 |
| 7 | Bu4NI instead of Bu4NBrd | <21 |
| 8 | Bu4NBF4 instead of Bu4NBrd | 44 |
| 9 | 0.8 equiv Bu4NBr instead of 2.4 equiv Bu4NBrd | 40 |
| 10 | 4.0 equiv Bu4NBr instead of 2.4 equiv Bu4NBrd | 43 |
| 11 | 0 °C instead of rt | 45 |
| 12 | 60 °C instead of rt | <44 |
| 13 | 20 mA instead of 12 mA, 1.0 F/mol | <33 |
| 14 | 6 mA instead of 12 mA, 1.0 F/mol | 46 |
| 15 | no electric current | n.d.c,e |
aStandard conditions: 1 (0.5 mmol), 0.3 M Bu4NBr in DMF (4.0 mL × 2), divided cell, 12 mA, rt, 1.0 F/mol of electricity against 0.5 mmol of substrate 1. bIsolated yields using preparative GPC separation of the crude materials. cObserved from gas chromatography (GC) analysis. dIn both anodic and cathodic chambers. en.d. = no detection.