Abstract

As an alternative to conventional asymmetric hydroformylation (AHF), asymmetric transfer hydroformylation (ATHF) by using formaldehyde as a surrogate for syngas is reported. A catalyst derived from commercially available [Rh(acac)(CO)2] (acac=acetylacetonate) and 1,2-bis[(2S,5S)-2,5-diphenylphospholano]ethane(1,5-cyclooctadiene) (Ph-BPE) stands out in terms of both activity and enantioselectivity. Remarkably, not only are high selectivities achievable, the reactions are very simple to perform, and higher enantioselectivity (up to 96 % ee) and/or turnover frequencies than those achievable by using the same catalyst (or other leading catalysts) can be obtained by using typical conditions for AHF.

Highlights

  • The development of catalytic reactions that make use of surrogates for carbon monoxide is currently experiencing intense research activity.[1]

  • Metric reagents and the surrogate is cheap; relatively few papers demonstrate these features.[1b,c] On this basis, the transfer hydroformylation of alkenes using formaldehyde is a potentially ideal transformation,[3] but had not been reported in an enantioselective fashion.[3c] we show that asymmetric transfer hydroformylation (ATHF) can, be carried out on low-reactivity alkenes, giving products in minutes, often with high enantioselectivity

  • At the onset of this work, we had found that some typical easy substrates for hydroformylation, such as mono-substituted vinyl arenes, did not seem suited to ATHF, because we obtained the linear isomer as the major product

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Summary

Introduction

The development of catalytic reactions that make use of surrogates for carbon monoxide is currently experiencing intense research activity.[1]. Ligands that give very reactive conventional enantioselective hydroformylation catalysts, such as Kelliphite[5a] and BOBPHOS,[5b] gave very low yields, (R,R)-Ph-BPE/[Rh(acac)(CO)2],[5c] stands out for ATHF. In the case of the cis-stilbene hydroformylation, we found that [RhCl(COD)]2 and Ph-BPE, as was used in Reference [3 c], was not an effective catalyst (2 % conversion), a significant amount of gas pressure built up (Table 1, entry 10).

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