Table 1. Optimization of the Reaction Conditions.
entry | catalyst | time [h] | 3aa [%]a | conv. [%]b |
---|---|---|---|---|
1 | 15 | 17 | 17 | |
2 | SO4/ZrO2 | 15 | 27 | 30 |
3 | Amberlyst 15DRY | 15 | 41 | 46 |
4 | Nafion-H | 15 | 45 | 52 |
5 | H-ZSM-5 | 15 | 27 | 28 |
6 | H–Y Zeolite | 15 | 66 | 75 |
7 | H-beta Zeolite | 15 | 58 | 62 |
8 | H-mordenite | 15 | 73 | 78 |
9 | H-mont | 15 | 77 | 85 |
10 | Fe-mont | 15 | 74 | 85 |
11 | Cu-mont | 15 | 60 | 68 |
12 | Zn-mont | 15 | 66 | 77 |
13 | Zr-mont | 15 | 73 | 80 |
14 | Sn-mont | 15 | 66 | 75 |
15 | H-mont | 24 | 81 | 88 |
16c | H-mont | 24 | 88 (86)d | 96 |
17 | PTSA·H2Oe | 15 | 47 | 84 |
Yield of 3aa was determined via gas chromatography (GC) analysis using n-tetradecane as an internal standard.
Conversion of 1a was determined via GC analysis.
2a (2.2 mmol) was used.
Isolated yield.
5 mol % was used.