Perera-Solis Diego D, Zholobenko Vladimir L, Whiting Andrew, Greenwell Hugh Christopher
Department of Chemistry, Durham University Durham DH1 3LE UK
Centre for Sustainable Chemical Processes, Department of Chemistry, Durham University Durham DH13LE UK.
RSC Adv. 2021 Nov 3;11(56):35575-35584. doi: 10.1039/d1ra06871g. eCollection 2021 Oct 28.
Ketonic decarboxylation has gained significant attention in recent years as a pathway to reduce the oxygen content within biomass-derived oils, and to produce sustainable ketones. The reaction is base catalysed, with MgO an economic, accessible and highly basic heterogeneous catalyst. Here we use MgO to catalyse the ketonic decarboxylation of dodecanoic acid to form 12-tricosanone at moderate temperatures (250 °C, 280 °C and 300 °C) with low catalyst loads of 1% (w/w), 3% (w/w) and 5% (w/w) with respect to the dodecanoic acid, with a reaction time of 1 hour under batch conditions. Three different particle sizes for the MgO were tested (50 nm, 100 nm and 44 μm). Ketone yield was found to increase with increasing reaction temperature, reaching approximately 75% yield for all the samples tested. Temperature was found to be the main control on reaction yield, rather than surface area or particle size.
近年来,酮式脱羧作为一种降低生物质衍生油中氧含量并生产可持续酮类的途径,受到了广泛关注。该反应由碱催化,氧化镁是一种经济、易得且碱性很强的非均相催化剂。在此,我们使用氧化镁在中等温度(250℃、280℃和300℃)下催化十二烷酸的酮式脱羧反应,以生成2-十三酮,相对于十二烷酸,催化剂负载量低至1%(w/w)、3%(w/w)和5%(w/w),在间歇条件下反应时间为1小时。测试了三种不同粒径的氧化镁(50nm、100nm和44μm)。发现酮产率随反应温度升高而增加,所有测试样品的产率均达到约75%。结果表明,温度是反应产率的主要控制因素,而非表面积或粒径。