Zhu Hongda, Jackson Timothy A, Subramaniam Bala
Center for Environmentally Beneficial Catalysis, University of Kansas, 1501 Wakarusa Dr., Lawrence, Kansas 66047, United States.
Department of Chemistry, University of Kansas, 1567 Irving Hill Rd, Lawrence, Kansas 66045, United States.
JACS Au. 2023 Feb 7;3(2):498-507. doi: 10.1021/jacsau.2c00631. eCollection 2023 Feb 27.
We have demonstrated the oxidation of mixed alkanes (propane, -butane, and isobutane) by ozone in a condensed phase at ambient temperature and mild pressures (up to 1.3 MPa). Oxygenated products such as alcohols and ketones are formed with a combined molar selectivity of >90%. The ozone and dioxygen partial pressures are controlled such that the gas phase is always outside the flammability envelope. Because the alkane-ozone reaction predominantly occurs in the condensed phase, we are able to harness the unique tunability of ozone concentrations in hydrocarbon-rich liquid phases for facile activation of the light alkanes while also avoiding over-oxidation of the products. Further, adding isobutane and water to the mixed alkane feed significantly enhances ozone utilization and the oxygenate yields. The ability to tune the composition of the condensed media by incorporating liquid additives to direct selectivity is a key to achieving high carbon atom economy, which cannot be achieved in gas-phase ozonations. Even in the liquid phase, without added isobutane and water, combustion products dominate during neat propane ozonation, with CO selectivity being >60%. In contrast, ozonation of a propane+isobutane+water mixture suppresses CO formation to 15% and nearly doubles the yield of isopropanol. A kinetic model based on the formation of a hydrotrioxide intermediate can adequately explain the yields of the observed isobutane ozonation products. Estimated rate constants for the formation of oxygenates suggest that the demonstrated concept has promise for facile and atom-economic conversion of natural gas liquids to valuable oxygenates and broader applications associated with C-H functionalization.
我们已经证明,在环境温度和温和压力(高达1.3兆帕)下,臭氧能在凝聚相中氧化混合烷烃(丙烷、丁烷和异丁烷)。形成了醇类和酮类等含氧化合物,其综合摩尔选择性大于90%。控制臭氧和氧气的分压,使气相始终处于可燃范围之外。由于烷烃 - 臭氧反应主要发生在凝聚相中,我们能够利用富含烃类的液相中臭氧浓度的独特可调性,轻松活化轻质烷烃,同时避免产物过度氧化。此外,向混合烷烃进料中添加异丁烷和水可显著提高臭氧利用率和含氧化合物产率。通过加入液体添加剂来调节凝聚介质的组成以指导选择性,是实现高碳原子经济性的关键,这在气相臭氧化中是无法实现的。即使在液相中,不添加异丁烷和水时,纯丙烷臭氧化过程中燃烧产物占主导,CO选择性大于60%。相比之下,丙烷 + 异丁烷 + 水混合物的臭氧化可将CO生成抑制至15%,并使异丙醇产率几乎翻倍。基于氢三氧化物中间体形成的动力学模型能够充分解释观察到的异丁烷臭氧化产物的产率。估计的含氧化合物形成速率常数表明,所展示的概念有望将天然气液体轻松且原子经济地转化为有价值的含氧化合物,并实现与C - H官能化相关的更广泛应用。