Zinc-free, Scalable Reductive Cross-Electrophile Coupling Driven by Electrochemistry in an Undivided Cell

被引:52
作者
Franke, Mareena C. [1 ]
Longley, Victoria R. [1 ]
Rafiee, Mohammad [2 ]
Stahl, Shannon S. [1 ]
Hansen, Eric C. [3 ]
Weix, Daniel J. [1 ]
机构
[1] Univ Wisconsin, Dept Chem, Madison, WI 53706 USA
[2] Univ Missouri, Dept Chem, Kansas City, MO 64110 USA
[3] Pfizer Inc, Chem Res & Dev, Groton, CT 06340 USA
关键词
nickel; electrochemistry; cross-coupling; flow; cross-electrophile coupling; mechanism; multimetallic catalysis; ARYL HALIDES; ALKYL-HALIDES; NICKEL CATALYSIS; CO-CATALYSIS; BROMIDES; ELECTROLYTE; TRANSITION; COMPOSITE; SYSTEM;
D O I
10.1021/acscatal.2c03033
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Nickel-catalyzed reductive cross-electrophile coupling reactions are becoming increasingly important in organic synthesis, but application at scale is limited by three interconnected challenges: a reliance on amide solvents (complicated workup, regulated), the generation of stoichiometric Zn salts (complicated isolation, waste disposal issue), and mixing/activation challenges of zinc powder. We show here an electrochemical approach that addresses these three issues: the reaction works in acetonitrile with diisopropylethylamine as the terminal reductant in a simple undivided cell [graphite(+)/nickel foam(-)]. The reaction utilizes a combination of two ligands, 4,4'-di-tert-butyl-2,2'-bipyridine and 4,4',4.-tritert-butyl-2,2':6',2.-terpyridine. Studies show that, alone, the bipyridine nickel catalyst predominantly forms the protodehalogenated aryl and aryl dimer, whereas the terpyridine nickel catalyst predominantly forms the bialkyl and product. By combining these two unselective catalysts, a tunable, general system results because excess radicals formed by the terpyridine catalyst can be converted to the product by the bipyridine catalyst. As the aryl bromide becomes more electron-rich, the optimal ratio shifts to have more of the bipyridine nickel catalyst. Finally, examination of a variety of flow-cell configurations establishes that batch recirculation can achieve higher productivity (mmol product/time/electrode area) than single-pass flow, that high flow rates are essential for maximizing current, and that two flow cells in parallel can nearly halve the reaction time. The resulting reaction is demonstrated on gram scale and should be scalable to kilogram scale.
引用
收藏
页码:12617 / 12626
页数:10
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