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烯烃的甲醇化反应:通过甲醇向烯烃的形式加成实现醇类的低压合成。

Methanolation of Olefins: Low-Pressure Synthesis of Alcohols by the Formal Addition of Methanol to Olefins.

作者信息

Stahl Sebastian, Vossen Jeroen T, Popp Stephan, Leitner Walter, Vorholt Andreas J

机构信息

Max Planck Institute for Chemical Energy Conversion, Stiftstraße 34-36, 45470, Mülheim an der Ruhr, Germany.

Institute for Technical and Macromolecular Chemistry, RWTH Aachen University, Worringerweg 2, 52074, Aachen, Germany.

出版信息

Angew Chem Int Ed Engl. 2025 Feb 10;64(7):e202418984. doi: 10.1002/anie.202418984. Epub 2024 Dec 4.

Abstract

Methanolation of olefins is introduced as a new low-pressure synthetic pathway to C1 elongated alcohols. Formally, HCOH is added to the C=C bond in a 100 % atom efficient manner. Mechanistically, the overall transformation occurs as a tandem reaction sequence by combining the dehydrogenation of methanol to syngas at a CO : H ratio of 1 : 2 with subsequent hydroformylation to the corresponding aldehyde and its final hydrogenation to the alcohol. The dehydrogenation and hydrogenation steps are catalyzed by a Mn/pincer complex, while the hydroformylation is accomplished by a Rh/phosphine catalyst. Using 1-octene as prototypical substrate, a yield of 80 % nonanol was achieved with a ratio of 93 : 7 of linear to branched alcohols and turnover numbers (TON) of more than 17 000 could be obtained in relation to the precious metal Rhodium. The integrated catalytic system provides direct access to alcohols from olefins and "green" methanol, avoiding the handling of pressurized CO and H and the use of specialized high-pressure equipment as the process conditions do not exceed 10 bar with partial pressures of syngas in the range of only 1-2 bar.

摘要

烯烃的甲醇化被引入作为一种合成 C1 链增长醇的新型低压合成途径。从形式上看,以 100% 的原子利用率将 HCOH 添加到 C=C 键上。从机理上讲,整个转化过程是通过将甲醇脱氢生成 CO:H 比为 1:2 的合成气,并随后进行氢甲酰化反应生成相应的醛,最后将醛氢化生成醇,以串联反应序列的形式发生。脱氢和氢化步骤由 Mn/钳形配合物催化,而氢甲酰化反应则由 Rh/膦催化剂完成。以 1-辛烯作为典型底物,壬醇的产率达到 80%,直链醇与支链醇的比例为 93:7,相对于贵金属铑,周转数(TON)可超过 17000。该集成催化系统可直接从烯烃和“绿色”甲醇制备醇,避免了处理加压的 CO 和 H,以及使用专门的高压设备,因为该工艺条件不超过 10 bar,合成气的分压仅在 1-2 bar 范围内。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/8f49/11811677/4efcd6368709/ANIE-64-e202418984-g007.jpg

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