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首页> 外文期刊>The Journal of Supercritical Fluids >Hydroformylation of styrene in supercritical carbon dioxide with fluoroacrylate polymer supported rhodium catalysts
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Hydroformylation of styrene in supercritical carbon dioxide with fluoroacrylate polymer supported rhodium catalysts

机译:含氟丙烯酸酯聚合物负载的铑催化剂在超临界二氧化碳中将苯乙烯加氢甲酰化

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摘要

Rhodium catalysts, bound to a fluoroacrylate copolymer backbone through phosphine ligands, are synthesized and shown to be soluble and active in supercritical carbon dioxide. Hydroformylation of styrene is studied using this catalyst at two different temperatures (323 and 348 K) and three different pressures (172, 207, and 241 bar). The initial mole fraction of styrene was 4.13 x 10(-4), styrene to Rh molar ratio was 200, and hydrogen and carbon monoxide to styrene molar ratio was 160. Conversions up to almost 100% and branched aldehyde selectivities of 95-100% were obtained at most reaction conditions. A kinetic model is proposed based on a dissociative mechanism, which starts by dissociation of a CO ligand to produce RRh(CO)(2)L-2. Then coordination of an olefin, insertion of hydrogen, and coordination of CO generates the alkylrhodium complex followed by CO insertion to generate the acyl complex. Finally, reductive elimination forms the aldehyde. Oxidative addition of hydrogen is proposed as the rate-control ling step. (C) 2004 Published by Elsevier B.V.
机译:合成了通过膦配体与氟丙烯酸酯共聚物主链结合的铑催化剂,并显示出其在超临界二氧化碳中的溶解性和活性。使用该催化剂在两个不同的温度(323和348 K)和三个不同的压力(172、207和241 bar)下研究了苯乙烯的加氢甲酰化。苯乙烯的初始摩尔分数为4.13 x 10(-4),苯乙烯与Rh的摩尔比为200,氢和一氧化碳与苯乙烯的摩尔比为160。转化率几乎达到100%,支链醛的选择性为95-100%在大多数反应条件下均可获得。提出了一种基于解离机理的动力学模型,该机理以CO配体解离开始产生RRh(CO)(2)L-2。然后,烯烃的配位,氢的插入和CO的配位生成烷基铑配合物,然后CO插入以生成酰基配合物。最后,还原消除形成醛。提议将氢的氧化加成作为速率控制步骤。 (C)2004由Elsevier B.V.发布

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