Table 1.
Optimisation for the carbonylation of ortho-substituted substrates in flow.
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| Entry | Ligand | Temperature (°C) | CO pressure (bar) | Conversion (%) | Isolated yield of 5 (%) |
| 1 | X-Phos | 110 | 5 | 68 | 31 |
| 2 | S-Phos | 110 | 5 | 43 | 36 |
| 3 | DPPB | 110 | 5 | 90 | 38 |
| 4 | Xantphos | 110 | 5 | 57 | 36 |
| 5 | PPh3 | 110 | 5 | 44 | 36 |
| 6a | PPh3 | 110 | 5 | 59 | 36 |
| 7b | PPh3 | 110 | 5 | 80 | 33 |
| 8c | PPh3 | 110 | 5 | N/D | 18 |
| 9 | PPh3 | 100 | 5 | 41 | 31 |
| 10 | PPh3 | 120 | 5 | 60 | 37 |
| 11 | PPh3 | 130 | 5 | N/D | 33 |
| 12d | PPh3 | 110 | 10 | 67 | 46 |
| 13d | PPh3 | 110 | 15 | 74 | 62 |
| 14d,e | PPh3 | 110 | 15 | N/D | 31 |
| 15f | PPh3 | 110 | 15 | N/D | 68 |
| 16f,a | PPh3 | 110 | 15 | 99 | 90 |
| 17f,b | PPh3 | 110 | 15 | 99 | 73 |
a1.6 equiv of base. b2.0 equiv of base. c1.1 equiv of DBU used instead of NEt3. d10 mL reactor was not “tube-in-tube”. e20 mol % DMF added. f2 × 15 mL “tube-in-tube” reactors used. N/D: not determined.
