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Unraveling high alkene selectivity at full conversion in alkyne hydrogenation over Ni under continuous flow conditions

机译:Unraveling high alkene selectivity at full conversion in alkyne hydrogenation over Ni under continuous flow conditions

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摘要

Selective hydrogenation of alkynes into alkenes under continuous flow conditions over non-precious metal catalysts is an attractive prospect for the chemical industry, especially for the petrochemical and polymer industry. Achieving high alkene selectivity at full alkyne conversions is an ongoing challenge. To address this, we dissolved carbon into Ni lattices by treating Ni@C material derived from MOF-74(Ni) with H2 at 300 °C and the resultant material is explored as a catalyst for selective styrene synthesis from phenylacetylene (PA) under fixed bed flow conditions. The designed catalyst exhibited a rare combination of sustained high styrene (ST) selectivity (92 ± 1%) and full phenylacetylene (PA) conversion (>99%). Density functional theory (DFT) calculations predict that the carbon incorporation decreases the interaction energy between ST and the catalyst surface, and this increased the reaction barrier for further hydrogenation. Time on stream data showed a 13 h stable performance and the catalyst is regenerable for 4 cycles without a loss of activity. Further, PA is completely removed (by semi-hydrogenation) from the styrene stream even when it is present in low quantities (1.8%).
机译:炔烃为烯烃的选择性加氢在连续流条件下结束了non-precious金属催化剂是一个有吸引力的化工行业的前景,尤其是石油化工和高分子行业。实现高烯烃选择性全炔转换是一个持续的挑战。这一点,我们溶解碳到镍晶格治疗Ni@C材料来自财政部- 74 (Ni)在300°C与H2和合成材料探索催化剂选择性的苯乙烯合成的苯乙炔(PA)在固定的床流条件。表现出一种罕见的持续高企的组合苯乙烯(ST)选择性(92±1%)和充实苯乙炔(PA)转换(> 99%)。泛函理论(DFT)计算预测碳的掺入降低了圣和催化剂之间的相互作用能表面,这增加了反应的障碍进一步加氢。显示一个13 h性能稳定,催化剂是可以再生4周期没有损失吗活动。从苯乙烯流甚至semi-hydrogenation)当它出现在低量(1.8%)。

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