Table 1. Optimization of Reaction Conditions in the Formation of 3aa.
entry | catalyst | base (aq.) | solvent T (°C) | time (days) | yield (%)b | dr (3a:3aa)c | ee (%)c | entry | catalyst | base (aq.) | solvent | T (°C) | time (days) | yield (%)b | dr (3a:3aa)c | ee (%)d,e |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
a | 4a | Na2CO3 | toluene 25 | 3 | 45 | 92:8 | 10 | l | 4e | NaOH | toluene | 25 | 1 | 20 | 90:10 | 5 |
b | 4b | Na2CO3 | toluene 25 | 2 | 60 | 93:7 | 5 | m | 4e | CsOH | toluene | 25 | 1 | 25 | 95:5 | 10 |
c | 4c | Na2CO3 | toluene 25 | 4 | 80 | 93:7 | 55 | n | 4e | Na2CO3 | xylene | 0 | 3 | 98 | 99:1 | 99 |
d | 4d | Na2CO3 | toluene 25 | 3 | 85 | 98:2 | 60 | o | 4e | Na2CO3 | toluene | 0 | 3 | 60 | 99:1 | 65 |
e | 4e | Na2CO3 | toluene 25 | 2 | 90 | 99:1 | 85 | p | 4e | Na2CO3 | MTBE | 0 | 3 | 50 | 99:1 | 30 |
f | 4f | Na2CO3 | toluene 25 | 4 | 40 | 95:5 | 50 | q | 4e | Na2CO3 | benzene | 0 | 3 | 55 | 99:1 | 40 |
g | 4g | Na2CO3 | toluene 25 | 5 | 45 | 89:11 | 30 | r | 4e | Na2CO3 | DCE | 0 | 3 | 35 | 99:1 | 20 |
h | 4h | Na2CO3 | toluene 25 | 4 | 50 | 88:22 | 25 | s | 4e | Na2CO3 | xylene | –20 | 4 | 35 | 99:1 | 40 |
i | 4i | Na2CO3 | toluene 25 | 5 | 40 | 90:10 | 30 | t | 4e | Na2CO3 | toluene | –40 | 5 | 30 | 99:1 | 30 |
j | 4e | K2CO3 | toluene 25 | 2 | 80 | 99:1 | 70 | u | 4e | Na2CO3 | toluene | –78 | 2 | |||
k | 4e | Cs2CO3 | toluene 25 | 2 | 65 | 95:5 | 20 |
All reactions were performed at 0.21 mmol of 1, 0.25 mmol of 2, 5 mol % 4e and 0.2 mL of aqueous base in 5 mL of solvent.
Isolated yields after column chromatography.
Diastereomeric ratio was determined by 1H NMR.
Enantiomeric excess was determined by chiral high-performance liquid chromatography (HPLC).
Enantiomeric ratio of the major diastereomer.