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Non-bridging zwitterionic half-metallocene complex and application thereof

A zwitterion, single metallocene technology, applied in the field of olefin polymerization catalysts, to achieve the effect of low catalytic cost

Inactive Publication Date: 2016-10-26
JILIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The closest prior art with the present invention is: Angewandte Chemie, 2011, 123 (8), 1905-1908; ACS Catalysis, 2011, 1 (11), 1637-1642 and Journal of the American Chemical Society, 2013, 135 (19 ), 7235-7250, although there are reports of some related zwitterionic metallocene complexes in this document, the reported complexes are mainly used to catalyze the intramolecular hydrogenation reaction of enamines, and have not yet been applied to catalyze olefin polymerization reactions. report

Method used

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  • Non-bridging zwitterionic half-metallocene complex and application thereof
  • Non-bridging zwitterionic half-metallocene complex and application thereof
  • Non-bridging zwitterionic half-metallocene complex and application thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0022] Embodiment 1 Synthesis of non-bridging zwitterionic single metallocene complexes

[0023]

[0024] At room temperature and under a nitrogen atmosphere, 2.05 mmol of NaH powder was slowly mixed with 20 mL of a THF solution containing 2.00 mmol of protonated organoborate ligands (one of HL1-HL10), and the reaction mixture was stirred at room temperature for 10 hours, and then The reaction solution was cooled to -20°C and filtered to remove insoluble matter. The resulting filtrate was added at -20°C to a solution containing an equivalent amount of monometallocene complex Cp'MX 2 (2.00 mmol) in THF (20 mL), stirred overnight at room temperature. The solvent was distilled off under reduced pressure, and the crude product was washed with CHCl 3 / n-Hexane mixed solvent recrystallization to obtain a blue-green product. Experimental results: complex I1, yield 0.542g, yield 50%, elemental analysis C 70.88, H 5.69, N 5.24; complex I2, yield 0.504g, yield 44%, elemental analys...

Embodiment 2

[0025] Embodiment 2 catalytic ethylene polymerization reaction

[0026] The polymerization reaction was carried out in a 250 mL autoclave, using the non-bridged zwitterionic monometallocene complexes I1-I9 and II1-II11 prepared in Example 1 above as main catalysts, and aluminum alkyls as co-catalysts. Before the polymerization reaction, the reactor was baked at 120° C. for 1 hour under vacuum, and filled with ethylene gas at an atmospheric pressure. Under an ethylene atmosphere, first 70mL of toluene solution containing the procatalyst (Al / M in Table 1 represents the molar ratio of the aluminum in the procatalyst to the metal in the procatalyst) was added to the reactor, and then 10mL of the procatalyst ( 2umol) of toluene solution was added to the reactor, the ethylene pressure was raised to 5 atmospheres, and the timing was started. After the polymerization reaction was carried out for 30 minutes, the ethylene gas in the reactor was vented, and the polymerization reaction w...

Embodiment 3

[0030] Embodiment 3 catalytic ethylene / norbornene copolymerization reaction

[0031] The polymerization reaction was carried out in a 250mL autoclave, using the non-bridged zwitterionic monometallocene complexes I1~I9 and II1~II11 prepared in the above Example 1 as the main catalyst, and the alkylaluminum or haloalkylaluminum as the cocatalyst . Before the polymerization reaction, the reactor was baked at 120° C. for 1 hour under vacuum, and filled with ethylene gas at an atmospheric pressure. Under an ethylene atmosphere, first add 70 mL of toluene solution containing cocatalyst and norbornene (NBE) into the reactor, then add 10 mL of toluene solution containing main catalyst (2 μmol) into the reactor, and raise the ethylene pressure to 5 atmospheric pressure and start the timer. After the polymerization reaction was carried out for 30 minutes, the ethylene gas in the reactor was vented, and the polymerization reaction was terminated with HCI / methanol solution. The polymer...

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Abstract

The invention relates to non-bridging zwitterionic half-metallocene complex and application thereof and belongs to the technical field of olefin polymerization catalysts. The general formula of the non-bridging zwitterionic half-metallocene complex is as shown in the specification. Ethylene homopolymerization and the copolymerization of ethylene and norbornene can be catalyzed by using the non-bridging zwitterionic half-metallocene complex as the main catalyst and aluminum alkyl and alkyl aluminium halide or the mixture of the aluminum alkyl and alkyl aluminium halide as the auxiliary catalyst. When the non-bridging zwitterionic half-metallocene complex is used as the catalyst of olefin polymerization, the non-bridging zwitterionic half-metallocene complex only needs to be activated by the aluminum alkyl, low catalyzing cost is achieved, and the non-bridging zwitterionic half-metallocene complex can be used for catalyzing ethylene homopolymerization and the copolymerization of the ethylene and norbornene.

Description

technical field [0001] The invention belongs to the technical field of olefin polymerization catalysts, in particular to the preparation of a non-bridged zwitterionic monometallocene complex and its use in catalyzing olefin polymerization, especially in catalyzing the homopolymerization of ethylene and the copolymerization of ethylene and norbornene Applications. Background technique [0002] Due to the advantages of low price, easy processing, good mechanical properties, and wide application fields, polyolefin products are widely used in various fields of human production and life, and have become the most widely used synthetic polymer materials in human society. With the development of society and the advancement of technology, people's requirements for the variety and quality of polyolefin products are also increasing, so new polyolefin products need to be continuously developed. The technical level of the production of polyolefin products mainly depends on the catalyst ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/00C08F110/02C08F210/02C08F232/08C08F4/69C08F4/639
CPCC08F4/63912C08F4/6392C08F10/00C08F110/02C08F210/02C08F2420/03C08F2420/06C08F232/08C08F2500/01
Inventor 母瀛张强李彪宋婷婷
Owner JILIN UNIV