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用于生产高性能生物基喷气燃料的异戊二烯[4+4]环加成反应

[4+4]-Cycloaddition of Isoprene for the Production of High-Performance Bio-Based Jet Fuel.

作者信息

Rosenkoetter Kyle E, Kennedy C Rose, Chirik Paul J, Harvey Benjamin G

机构信息

US NAVY, NAWCWD, Research Department, Chemistry Division, China Lake, California 93555.

Department of Chemistry, Princeton University, Princeton, New Jersey 08544, United States.

出版信息

Green Chem. 2019 Oct 21;21(20):5616-5623. doi: 10.1039/c9gc02404b. Epub 2019 Sep 6.

Abstract

Isoprene was efficiently converted to 1,6-dimethyl-1,5-cyclooctadiene (DMCOD) by selective [4+4]-cycloaddition with a catalyst formed by in situ reduction of [(PI)FeCl(μ-Cl)] (PI = [2-(2,6-(CH)-CH-N=C(CH))-CHN]). DMCOD was isolated in 92% yield, at the preparative scale, with a catalyst loading of 0.025 mol%, and a TON of 3680. Catalytic hydrogenation of DMCOD yielded 1,4-dimethylcyclooctane (DMCO). The cyclic structure and ring strain of DMCO afforded gravimetric and volumetric net heats of combustion 2.4 and 9.2% higher, respectively, than conventional jet fuel. In addition, the presence of methyl branches at two sites resulted in a -20 °C kinematic viscosity of 4.17 mm s, 48 % lower than the maximum allowed value for conventional jet fuel. The ability to derive isoprene and related alcohols readily from abundant biomass sources, coupled with the highly efficient [Fe]-catalyzed [4+4]-cycloaddition described herein, suggests that this process holds great promise for the economical production of high-performance, bio-based jet fuel blendstocks.

摘要

通过与由[(PI)FeCl(μ-Cl)](PI = [2-(2,6-(CH)-CH-N=C(CH))-CHN])原位还原形成的催化剂进行选择性[4+4]环加成反应,异戊二烯被高效转化为1,6-二甲基-1,5-环辛二烯(DMCOD)。在制备规模下,以0.025 mol%的催化剂负载量,DMCOD的分离产率为92%,TON为3680。DMCOD的催化氢化反应生成1,4-二甲基环辛烷(DMCO)。DMCO的环状结构和环张力使其燃烧的重量净热和体积净热分别比传统喷气燃料高2.4%和9.2%。此外,在两个位置存在甲基支链导致其运动粘度在-20°C时为4.17 mm²/s,比传统喷气燃料允许的最大值低48%。能够从丰富的生物质来源轻松获得异戊二烯及相关醇类,再加上本文所述的高效[Fe]催化的[4+4]环加成反应,表明该过程在经济生产高性能生物基喷气燃料调合组分方面具有巨大潜力。

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