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Structure/activity relationships applied to the hydrogenation of α,β-unsaturated carbonyls: The hydrogenation of 3-butyne-2-one over alumina-supported palladium catalysts

机译:应用于α,β-不饱和羰基氢化的结构/活性关系:3-丁炔-2-酮在氧化铝负载钯催化剂上的氢化

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摘要

The gas phase hydrogenation of 3-butyne-2-one, an alkynic ketone, over two alumina-supported palladium catalysts is investigated using infrared spectroscopy in a batch reactor at 373 K. The mean particle size of the palladium crystallites of the two catalysts are comparable (2.4 ± 0.1 nm). One catalyst (Pd(NO3)2/Al2O3) is prepared from a palladium(II) nitrate precursor, whereas the other catalyst (PdCl2/Al2O3) is prepared using palladium(II) chloride as the Pd precursor compound. A three-stage sequential process is observed with the Pd(NO3)2/Al2O3 catalyst facilitating complete reduction all the way through to 2-butanol. However, hydrogenation stops at 2-butanone with the PdCl2/Al2O3 catalyst. The inability of the PdCl2/Al2O3 catalyst to reduce 2-butanone is attributed to the inaccessibility of edge sites on this catalyst, which are blocked by chlorine retention originating from the catalyst’s preparative process. The reaction profiles observed for the hydrogenation of this alkynic ketone are consistent with the site-selective chemistry recently reported for the hydrogenation of crotonaldehyde, an alkenic aldehyde, over the same two catalysts. Thus, it is suggested that a previously postulated structure/activity relationship may be generic for the hydrogenation of α,β-unsaturated carbonyl compounds over supported Pd catalysts.
机译:在373 K的间歇反应器中,使用红外光谱研究了在两种氧化铝负载的钯催化剂上3-烷基炔酮的3-丁炔-2-酮的气相加氢反应。两种催化剂的钯微晶的平均粒径为可比的(2.4±0.1 nm)。一种催化剂(Pd(NO3)2 / Al2O3)由硝酸钯(II)前体制备,而另一种催化剂(PdCl2 / Al2O3)使用氯化钯(II)作为Pd前体化合物制备。 Pd(NO3)2 / Al2O3催化剂促进了完全还原成2-丁醇的过程,观察到一个三阶段的顺序过程。但是,用PdCl2 / Al2O3催化剂在2-丁酮处氢化停止。 PdCl2 / Al2O3催化剂无法还原2-丁酮的原因是该催化剂上的边缘部位难以接近,这些边缘部位被催化剂制备过程中的氯余留所阻止。观察到的对该炔酮的氢化反应的反应曲线与最近报道的在相同的两种催化剂上巴豆醛(一种烯醛)的氢化的定点化学相一致。因此,建议对于负载型Pd催化剂上的α,β-不饱和羰基化合物的氢化,先前假定的结构/活性关系可能是通用的。

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