Ethylene oligomerization catalyst composition and application thereof

Abstract

The invention relates to an ethylene oligomerization catalyst composition which comprises a chloride 2-benzoxazolyl-6-acetyl condensed amino ferrite (II) complex shown in formula I, an aluminum-containing promoter and tert-butyl hydroperoxide. The invention further provides an ethylene oligomerization method. The ethylene oligomerization catalyst composition provided by the invention is applied to ethylene oligomerization, and is high in reaction activity at low temperature in the presence of low Al / Fe, that is, the reaction activity is up to 1.62*10<7>g.mol (Fe)<1>.h<1>.

Description

technical field [0001] The invention relates to the field of ethylene oligomerization, in particular to an ethylene oligomerization catalyst composition containing an acetylamide iron complex and an application thereof. Background technique [0002] Linear α-olefins are widely used in the fields of ethylene comonomers, surfactant synthesis intermediates, plasticizer alcohols, synthetic lubricating oils and oil additives. In recent years, with the continuous development of the polyolefin industry, the worldwide demand for α-olefins has grown rapidly. At present, the vast majority of α-olefins are prepared by ethylene oligomerization. The used catalyst of ethylene oligomerization mainly contains nickel series, chromium series, zirconium series and aluminum series etc., in recent years, Brookhart group (Brookhart, M et al, J.Am.Chem.Soc.,1998,120,7143-7144 ; WO99 / 02472,1999), Gibson group (Gibson, V.C.et al, Chem.Commun.,1998,849-850; Chem.Eur.J.,2000,2221-2231) found some Fe...

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Problems solved by technology

[0003] The Institute of Chemistry, Chinese Academy of Sciences reported a catalyst for ethylene oligomerization and polymerization (Eur.J.Inorg.Chem.2009,4149–4156), which is 2-benzoxazolyl-6-acetylcondensate Amine Fe 2+ Chloride, under the action of co-catalyst methyl aluminoxane, when the molar ratio of the metal aluminum in the co-catalyst to the central metal in the main catalyst is 200-2000, and the reaction temperature is 30-50 ° C, oligomerization and Polymerization activity up to 10 7 g mol(Fe) -1 h -1 ; and whether methylalumoxane or modified methylalumoxane is used as a cocatalyst, the cost is too high and the consumption is too large. When the cocatalyst is used in large-scale ethylene oligomerization, it will inevitably lead to high cost

[0004] At present, it is generally believed that water and oxygen are very unfavorable to the ethylene oligomerization process. CN200810111717.8 discloses a method for ethylene oligomerization, which is strictly controlled in an anhydrous and oxygen-free environment. Therefore, the current ethylene oligomerization reaction The process requirements are very harsh, resulting in very poor reaction initiation and repeatability of the oligomerization process

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