Kyler Virtue, Babak Fayyaz, Francisco López-Linares, Oleg Mironov, Cesar Ovalles, Wesley Bernskoetter
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引用次数: 0
Abstract
CO2-based hydroesterification is an attractive route to produce value added ester compounds, which could replace CO-based hydroesterification processes if sufficient catalytic technologies are developed. One path to CO2-based hydroesterification is through an organoformate intermediate, which is then used in olefin hydroesterification to generate the desirable esters. This route creates a net CO2-based hydroesterification process using tandem catalytic systems for CO2 hydrogenation to organoformate paired with formate-olefin hydroesterification. The tandem use of tripodal phosphine ruthenium(II) and 1,2-bis(di-tert-butylphosphinomethyl)benzene palladium catalysts were found to successfully produce methyl nonanoate from CO2, H2, methanol and 1-octene in a single-stage batch process. The CO2-based hydroesterification catalysis efficiency was found to be largely limited by the productivity of organoformate generation and competitive 1-octene reduction. Catalytic yields of methyl nonanoate can be enhanced by adjustments in reaction procedures, including the use of a two-stage batch reaction process or delayed introduction of 1-octene, achieving a yield of up to 32%. Under select conditions, control experiments indicate yields of methyl nonanoate can be improved to ca 75%. Preliminary studies indicate significant interplay between the two ligands employed in the molecular tandem catalytic systems and establish the first catalytic protocol for the selective CO2-based hydroesterification of olefins via organoformates.
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