2014
DOI: 10.1016/j.jcat.2014.06.013
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Understanding the role of aluminum-based activators in single site iron catalysts for ethylene oligomerization

Abstract: In a combined experimental and theoretical study the activation process of a single site ethylene oligomerization catalyst with aluminum based activators has been studied.The results put forward a plausible deactivation reaction path of the catalyst for trimethylaluminum, while for methylaluminoxane and a novel phenoxyaluminum-based activator the experimental catalyst's activity correlates with the energy barrier for the ethylene insertion. Graphical AbstractN N N Fe N N N Fe Al Al Cl TMA MAO or [PhOAlMe 2 ] 2… Show more

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Cited by 27 publications
(32 citation statements)
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“…[196,197] Bringing this material into contact with (nBu 3 P) 2 NiCl 2 generates active ethylene dimerization catalysts with TOFs up to 498 000 mol C2H4 mol Ni À1 h À1 when MCM-41 is used as as upport (Scheme 8c). [198] [198] …”
Section: Well-defined Supported Ni Oligomerization Catalystsmentioning
confidence: 99%
“…[196,197] Bringing this material into contact with (nBu 3 P) 2 NiCl 2 generates active ethylene dimerization catalysts with TOFs up to 498 000 mol C2H4 mol Ni À1 h À1 when MCM-41 is used as as upport (Scheme 8c). [198] [198] …”
Section: Well-defined Supported Ni Oligomerization Catalystsmentioning
confidence: 99%
“…Beim Kontakt mit ( n Bu 3 P) 2 NiCl 2 bildet dieses Material aktive Ethylendimerisierungskatalysatoren mit TOFs bis 498 000 mol C2H4 mol Ni −1 h −1 , wenn MCM‐41 als Träger verwendet wird (Schema c) . Die Reaktion von ( n Bu 3 P) 2 NiCl 2 mit SBA‐15‐fixiertem Triethylaluminium, das auch dimere Spezies enthält, liefert einen Katalysator, der bei der Oligomerisation von Ethylen inaktiv ist – ein Hinweis darauf, dass chlorverbrückte Al‐Zentren wahrscheinlich bei dem Aktivierungsvorgang eine wichtige Rolle spielen, vermutlich über die Entstehung von Metall‐Ionen‐Paaren, die keine Ni,Al‐Dimetallspezies mit kurzen Methylbrücken bilden können …”
Section: Alken‐oligomerisationunclassified
“…However, the resulting ethylene oligomers of such BIP‐Fe catalysts are usually featured with a very broad distribution ranging from C 4 to C 30+ . And the proportion of polymers, can be higher than 40 wt% in the total products even the iron complexes with mono ortho ‐methyl substituted BIP ligands were employed . These undesired insoluble polymers would cause reactor fouling and pipeline blockage in a continuous process, which is a potential obstacle for the industrialization of the BIP‐Fe catalysts.…”
Section: Introductionmentioning
confidence: 99%