Journal
GREEN CHEMISTRY
Volume 24, Issue 17, Pages 6578-6588Publisher
ROYAL SOC CHEMISTRY
DOI: 10.1039/d2gc01252a
Keywords
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Funding
- European Union [817612]
- Max Planck Society
- H2020 Societal Challenges Programme [817612] Funding Source: H2020 Societal Challenges Programme
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Efficient transformation protocols using ethylene glycol as a solvent, along with rhodium catalysts and amines as catalysts, can convert linear alpha olefins to alcohols. By incorporating amine functionality into the solvent, the reaction system can be simplified and achieve high catalytic activity. Amine functionalized PEG derivatives are used to immobilize the rhodium catalyst, and supercritical CO(2) is used as the extracting solvent for product alcohol recycling, without any loss in activity or selectivity.
Efficient transformation protocols to directly convert olefins to alcohols are highly sought after. Ethylene glycol based solvents have proved to support the reductive hydroformylation of linear alpha olefins to alcohols using [Rh(acac)(CO)(2)] in combination with tertiary amines as catalysts. Incorporation of the amine functionality into the solvent using 2-[2-(dimethylamino)ethoxylethanol allowed simplification of the reaction system to three components and a catalytic activity with a TOF of 280 h(-1) for the reductive hydroformylation of 1-octene to be achieved. To immobilize the rhodium catalyst in a recycling approach using scCO(2) as the extracting solvent for product alcohols, amine functionalized PEG derivatives have been synthesized as the stationary catalyst phase. Amide condensation of PEG(600)-diacid with trimethyldiaminoethane resulted in a diaminated PEG(600) in which the amine group is linked via an amide bridge to the PEG(600) backbone. During nine consecutive runs, in which this PEG(600-)diamine was used as the stationary catalyst phase and product alcohols have been extracted with scCO(2), no loss in activity or selectivity was observed. Leaching of the stationary phase was <= 3 wt% (<= 0.5 wt% after the first two runs) of the extracted mass per run and rhodium leaching was determined to be 0.1% of the initial rhodium over all nine runs combined.
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