Shu-jie Chen,
Guo-ping Lu and
Chun Cai*
Chemical Engineering College, Nanjing University of Science & Technology, 200 Xiaolingwei, Nanjing, Jiangsu 210094, P. R. China. E-mail: c.cai@mail.njust.edu.cn
First published on 20th January 2015
A simple homogeneous catalyst system based on commercially available [IrCp*Cl2]2 has been developed for the conjugate reduction of α,β-unsaturated ketones. Under the optimized conditions, a wide range of α,β-unsaturated ketones were reduced to saturated ketones in 83–98% yield. While switching the base from K2CO3 to KOH, saturated alcohols was selectively obtained.
Despite all these advances, considering the constitution of these catalyst systems, most of the catalysts required tedious steps of synthesis or additive ancillary ligands. Only a few processes directly applied the commercially available catalyst, and most of them also suffered from drawbacks such as low yields, high temperature, and the use of toxic solvents.8,9 In this respect, the search for simple and practical catalyst system especially consisting of commercially available catalyst is still in high demand.
As part of our continuing interest in homogeneous iridium catalysts for organic transformations,14 we herein reported the potential of commercial available catalyst [IrCp*Cl2]2 in transfer hydrogenation of α,β-unsaturated ketones with 2-propanol as hydrogen source and solvent.
We began our studies by utilizing chalcone 1a as a model substrate in the presence of [IrCp*Cl2]2 (ref. 15) under various conditions (Table 1). Treatment of 1a with catalytic amount of [IrCp*Cl2]2 and K2CO3 in MeOH at 85 °C for 5 h gave the conjugate reduction product 2a in 31% yield with none of the double hydrogenation product 3a (Table 1, entry 1). A screening on other straight-chain fatty alcohols, that is, EtOH, 1-PrOH, and 1-BuOH, gave 2a in 36%, 70%, and 57% yields, respectively (entries 2–4). To our delight, when 2-PrOH was used, the reaction proceeded smoothly, yielding the 2a in 92% yield with excellent chemoselectivity (entry 5). To further improve the yield, a series of bases was then screened and Na2CO3 gave the similar result to K2CO3 (entry 6). Interestingly, in the case of Cs2CO3, the generated 2a was further hydrogenated to the saturated alcohol 3a in 64% yield (entry 7). Other strong bases, such as KOH and NaOH, gave 3a in 86, 84% yields, respectively (entries 8 and 9). Organic base NEt3 exhibited inhibitory effect on the reaction and resulted in a low yield (entry 10). It should be noted that decreasing the amount of K2CO3 to 5 mol% led to full conversion of 1a and 99% of the 2a was obtained within 5 h (Table 1, entry 11). However, in the absence of K2CO3, the reaction proceeded sluggishly (entry 12).
![]() | (1) |
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| Entry | Solvent | Base | Yieldb (%) | |
|---|---|---|---|---|
| 2a | 3a | |||
| a Reactions conditions: 1a (0.2 mmol), [IrCp*Cl2]2 (1 mol%), base (0.5 equiv.), solvent (1 mL), 85 °C, 5 h.b GC yield.c 5 mol% K2CO3 was used. Cp*: 1,2,3,4,5-pentamethylcyclopentadiene. | ||||
| 1 | MeOH | K2CO3 | 31 | 0 |
| 2 | EtOH | K2CO3 | 36 | 0 |
| 3 | 1-PrOH | K2CO3 | 70 | 0 |
| 4 | 1-BuOH | K2CO3 | 57 | 0 |
| 5 | 2-PrOH | K2CO3 | 92 | 0 |
| 6 | 2-PrOH | Na2CO3 | 89 | 0 |
| 7 | 2-PrOH | Cs2CO3 | 16 | 64 |
| 8 | 2-PrOH | KOH | 2 | 86 |
| 9 | 2-PrOH | NaOH | 3 | 84 |
| 10 | 2-PrOH | NEt3 | 14 | 0 |
| 11c | 2-PrOH | K2CO3 | 99 | 0 |
| 12 | 2-PrOH | — | 66 | 0 |
Base on the above findings and the literature data, we inferred that the role of the base was to generate a highly active Cp*IrH2 catalyst from the dichloride (eqn (1) and (2)).16 In addition, an excess of base resulted in low solubility of the substrate, which ultimately led to low yield. To validate our assumption, a series of controlled experiments based on the volume of 2-PrOH was carried out under the condition of entry 5, as showed in Fig. 1. As expected, the yield of 2a was merely moderate when the concentration of K2CO3 was high. Increasing the volume of 2-PrOH improved the yield of 2a. A full conversion of 1a and 99% yield of 2a was achieved when the amount of 2-PrOH was increasing to 2 mL. Continue increasing the volume of 2-PrOH to 5 mL did not change the yield of 2a.
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| Fig. 1 Effect of the volume of 2-PrOH on the catalytic transfer hydrogenation of chalcone with [IrCp*Cl2]2. | ||
With the optimized conditions in hands, various α,β-unsaturated ketones were then subjected to the reaction to establish the scope and generality of this protocol (Table 2). Firstly, a series of substituted chalcones were investigated (entries 2–16). The chalcones bearing electron-donating group Me and MeO on the 4′ position respectively required a higher catalyst loading and temperature to achieve satisfactory results (entries 2 and 3); while the chalcones bearing Me and MeO groups on the 4 position respectively were easy to reduce cleanly (entries 10 and 11). The transformations of halogen- and trifluoromethyl-substituted chalcones afforded desired products in 92–98% yields, and the position of the substituted groups did not significantly affect the reactivity (entries 4–7, 12–15). A similar result was observed in the case of 4′,2-disubstituted chalcone (entry 16). We also studied the cases of heterocyclic α-enones. To our delight, it still exhibited high activity and good selectivity, provided the desired products in excellent yields (entries 17 and 18). When the R2 group was occupied by H or alkyl groups, the reaction also proceeded smoothly in good to excellent yields (entries 19–21). Activated α,β-unsaturated ketones 1v and 1w, which have been proved to be good substrates in the previous reports, were also reduced in high yields (entries 22 and 23). Furthermore, the present catalytic system also displayed high catalytic efficiency for the reduction of cyclic enones (entries 24 and 25). However, α,β,γ,ε-unsaturated enone 1z was proved to be sluggish substrate and only trace amount of 2z was observed (entry 26). The transfer hydrogenations of α,β-unsaturated ketones to the corresponding alcohols were also investigated by applying KOH as the base. As expected, the desired saturated alcohols were obtained in 78–92% yields, which established our findings on the base-controlled chemoselectivity (entries 1–12, 22). Finally, an α,β-unsaturated ketone 1aa bearing a non-polarized double bond was subjected to the condition (eqn (3)). To our delight, the present catalytic system selectively reduced the enone and kept the non-polarized double bond.
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| Entry | 1 | R1 | R2 | Yield (%) | |
|---|---|---|---|---|---|
| 2b | 3c | ||||
| a Condition A: 1 (0.4 mmol), [IrCp*Cl2]2 (1 mol%), K2CO3 (5 mol%), 2-PrOH (4 mL), 85 °C, 5 h; condition B: 1 (0.4 mmol), [IrCp*Cl2]2 (1 mol%), KOH (50 mol%), 2-PrOH (4 mL), 85 °C, 5 h.b Isolated yield.c Yields were determined by GC analysis using n-hexadecane as internal standard (yield in parentheses is the isolated yield).d [IrCp*Cl2]2 (2 mol%), K2CO3 (10 mol%), 100 °C, 10 h.e 8 h. | |||||
| 1 | 1a | Ph | Ph | 97 (2a) | 88 (82) |
| 2d | 1b | p-MeC6H4 | Ph | 90 (2b) | 83 |
| 3d | 1c | p-MeOC6H4 | Ph | 85 (2c) | 78 |
| 4 | 1d | p-FC6H4 | Ph | 92 (2d) | 85 |
| 5 | 1e | p-ClC6H4 | Ph | 98 (2e) | 91 |
| 6 | 1f | p-BrC6H4 | Ph | 92 (2f) | 88 |
| 7 | 1g | m-ClC6H4 | Ph | 94 (2g) | 84 |
| 8 | 1h | o-MeC6H4 | Ph | 96 (2h) | 90 |
| 9 | 1i | 2-Naphthyl | Ph | 95 (2i) | 85 |
| 10 | 1j | Ph | p-MeC6H4 | 94 (2j) | 84 |
| 11 | 1k | Ph | p-MeOC6H4 | 93 (2k) | 85 |
| 12 | 1l | Ph | p-ClC6H4 | 97 (2l) | 89 |
| 13 | 1m | Ph | p-CF3C6H4 | 96 (2m) | |
| 14 | 1n | Ph | m-CF3C6H4 | 95 (2n) | |
| 15 | 1o | Ph | o-CF3C6H4 | 94 (2o) | |
| 16 | 1p | p-ClC6H4 | o-CF3C6H4 | 93 (2p) | |
| 17 | 1q | Furanyl | Ph | 93 (2q) | |
| 18 | 1r | Thiophenyl | Ph | 97 (2r) | |
| 19 | 1s | Ph | H | 87 (2s) | |
| 20 | 1t | Ph | Ph(CH2)2 | 96 (2t) | |
| 21 | 1u | Ph | CH3(CH2)5 | 94 (2u) | |
| 22 | 1v | Me | Ph | 95 (2v) | 92e |
| 23 | 1w | Me | Furanyl | 94 (2w) | |
| 24 | 1x | –C3H6– | 91 (2x) | ||
| 25 | 1y | –C2H4– | 97c (2y) | ||
| 26 | 1z | Ph | PhCH CH |
Trace (2z) | |
A plausible mechanism is proposed in Scheme 1 to explain the selective transfer hydrogenation of α,β-unsaturated ketones to the saturated ketones or alcohols.17 In the initial step, the active catalyst A was generated via the sequences showed in eqn (1) and (2). The α-enone 1a then coordinated to A, followed by a hydride transfer to give intermediate B, which underwent an enolization to produce C. The resulting Ir-enolate C was protonated by 2-PrOH to give product 2a and produced the catalytic species D, which sequently underwent a β-elimination to reproduce the active catalyst A. Although detailed mechanism for the secondary hydrogenation of the resulting ketones in the presence of KOH is not clear. A base promoted Meerwein–Ponndorf–Verley type reaction may be responsible for this unexpected results.18 More detailed studies are required to clarify the detailed mechanism.
:
5 to 90
:
10) to yield the product 2.
Footnote |
| † Electronic supplementary information (ESI) available: Experimental details, 1H-NMR, 13C-NMR, and 19F-NMR spectra of all isolated products. See DOI: 10.1039/c5ra00484e |
| This journal is © The Royal Society of Chemistry 2015 |