Mannel David S, Stahl Shannon S, Root Thatcher W
Department of Chemical and Biological Engineering and Department of Chemistry, University of Wisconsin-Madison , Madison, Wisconsin 53706, United States.
Org Process Res Dev. 2014 Nov 21;18(11):1503-1508. doi: 10.1021/op5002676. Epub 2014 Sep 23.
Ru(OH) /AlO is among the more versatile catalysts for aerobic alcohol oxidation and dehydrogenation of nitrogen heterocycles. Here, we describe the translation of batch reactions to a continuous-flow method that enables high steady-state conversion and single-pass yields in the oxidation of benzylic alcohols and dehydrogenation of indoline. A dilute source of O (8% in N) was used to ensure that the reaction mixture, which employs toluene as the solvent, is nonflammable throughout the process. A packed bed reactor was operated isothermally in an up-flow orientation, allowing good liquid-solid contact. Deactivation of the catalyst during the reaction was modeled empirically, and this model was used to achieve high conversion and yield during extended operation in the aerobic oxidation of 2-thiophene methanol (99+% continuous yield over 72 h).
Ru(OH) /AlO 是用于需氧醇氧化和氮杂环脱氢的用途较为广泛的催化剂之一。在此,我们描述了将间歇反应转化为连续流动方法的过程,该方法能够在苄醇氧化和二氢吲哚脱氢反应中实现高稳态转化率和单程产率。使用稀氧源(氮气中含8%氧气)以确保在整个过程中,以甲苯为溶剂的反应混合物不可燃。填充床反应器在向上流动的方向上进行等温操作,以实现良好的液 - 固接触。通过经验对反应过程中催化剂的失活进行建模,并利用该模型在2 - 噻吩甲醇的需氧氧化延长操作期间实现了高转化率和产率(72小时内连续产率超过99%)。