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Acetone alkylation with ethanol over multifunctional catalysts by a borrowing hydrogen strategy

机译:借用氢策略在多功能催化剂上用乙醇进行丙酮烷基化

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Step by step alkylation of acetone (A) with ethanol (E) in a ratio of 1 : 2 was investigated. A fixed bed flow-through reactor system was used at a total pressure of 21 bar and in the temperature range of 150-350 degrees C in inert He or a reducing H-2 medium. Following the hydrogen borrowing methodology, two types of catalysts were prepared; using neutral activated carbon (AC) and alkaline hydrotalcite (HT) supports, namely 5 wt% Pd/AC in the presence of alkaline additives (10, 20 and 30 wt% KOH or 20% K3PO4); 9 wt% Cu/HT and 5 wt% Pd/HT. The catalysts were activated in a H-2 flow at 350 degrees C. Different yields of mono- or dialkylated ketones were observed. In a hydrogen medium over the same catalyst systems the ketone products could be reduced to alcohols. In this study the Pd/HT catalyst seems to be the most promising for fuel production based on biomass fermentation.
机译:研究了丙酮(A)与乙醇(E)以1:2的比例逐步烷基化。在惰性He或还原性H-2介质中,在21 bar的总压力和150-350℃的温度范围内使用固定床流通式反应器系统。按照氢借入方法,制备了两种类型的催化剂:在碱性添加剂(10、20和30 wt%KOH或20%K3PO4)存在下,使用中性活性炭(AC)和碱性水滑石(HT)载体,即5 wt%Pd / AC; 9wt%的Cu / HT和5wt%的Pd / HT。催化剂在350℃下在H-2气流中活化。观察到单或二烷基化酮的收率不同。在相同催化剂体系上的氢气介质中,酮产物可还原为醇。在这项研究中,Pd / HT催化剂似乎是基于生物质发酵的燃料生产中最有前途的催化剂。

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