CN109957049A - Asymmetric (alpha-diimine) nickel alkene catalyst and its preparation method and application - Google Patents

Asymmetric (alpha-diimine) nickel alkene catalyst and its preparation method and application Download PDF

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CN109957049A
CN109957049A CN201711419028.9A CN201711419028A CN109957049A CN 109957049 A CN109957049 A CN 109957049A CN 201711419028 A CN201711419028 A CN 201711419028A CN 109957049 A CN109957049 A CN 109957049A
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methyl
isopropyl
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benzhydryl
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Shaoxing Pinghe New Materials Technology Co ltd
Hangzhou Xinglu Technology Co Ltd
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Hangzhou Star Road Technology Co Ltd
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    • C07F15/00Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table
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Abstract

The invention discloses a kind of based on asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance and its preparation method and application that 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone is skeleton.Shown in structural formula such as formula (I) based on asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance that 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone is skeleton of the invention.Wherein R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl or methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups, R4For methyl, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl, X is chlorine or bromine.The catalyst preparation process is simple, can under the action of co-catalyst catalyzed ethylene polymerization, show preferable thermal stability and polymerization activity, have good prospects for commercial application.

Description

Asymmetric (alpha-diimine) nickel alkene catalyst and its preparation method and application
Technical field:
The present invention relates to asymmetric (alpha-diimine) nickel alkene catalyst and its preparation method and application, especially a kind of bases In asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance that 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone is skeleton, Also relate to the preparation of the nickel alkene catalyst and the application of catalyzed polyeolfin.
Technical background:
Polyolefin is the basic material to involve the interests of the state and the people, and due to its excellent performance, the multiplicity of kind, raw material is easy It obtains and cheap, it is made to be widely used in each fields such as industry, agricultural and national defence.The development and application of raw catelyst is to push away Dynamic one of polyolefin industrial progress and the core drive of development are the key that the structure and performance for controlling polyolefine material.
In recent decades, it has been obtained widely by the research that coordination polymerization obtains functionalization and differential polyolefine material Concern.The Ni (II) and Pd for Brookhart research group discovery ligand containing alpha-diimine that nineteen ninety-five is subsidized by E.I.Du Pont Company (II) thus metal complex can develop the rear transition of a new generation at heavy polymer by catalyzed ethylene polymerization under normal pressure Metallic catalyst (J.Am.Chem.Soc., 1995,117 (23): 6414-6415).This kind of alpha-diimine nickel alkene catalyst Shown in specific structure such as formula (IV):
Up to the present, a large amount of research work keep two (aryl) alpha-diimine ligands layout it is constant in the case where, Group (R group of formula) on the neighboring group (R' in formula) and diimine skeleton of aryl is modified.When R' is from different When propyl changes methyl into, the degree of branching and molecular weight of resulting polymers are all reduced, and topological structure is more linear.However, this The thermal stability of class catalyst is poor, even if using the sub-polyethylene of this kind of catalyst preparation when R' is the isopropyl of big steric hindrance Son amount and catalyst activity all sharply decline with the rising of temperature.When polymerization temperature rises above 60 DEG C, catalyst is heated It decomposes rapidly and inactivates.Rieger (J.AM. CHEM.SOC., 2007,129,9182-9191), Long (J.AM.CHEM.SOC., 2013,135,16316-16319;ACS Catalysis, 2014,4,2501-2504) et al. by R' Aryl or substituted aryl are become by alkyl, prepared catalyst thermal stability increases substantially, when polymerization temperature is higher than 60 DEG C when, catalyst still maintains good catalytic activity.But, this two sides aniline substituent group is what bulky substituent was rolled into a ball The catalyst of symmetrical structure, when the ligand for preparing catalyst, since steric hindrance is big, the yield of ligand is very low, leads Cause the synthesis cost of catalyst high;Meanwhile the R' of bulky substituent group hinders the quick insertion of ethylene, causes When catalyzed ethylene polymerization, the polymerization activity of catalyst is not high, limits its industrial applications.
Summary of the invention:
It is a kind of based on 9,10- dihydro -9,10- ethylene anthracene-the purpose of the present invention is overcoming the deficiencies of the prior art and provide 11,12- diketone is asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance of skeleton and its preparation method and application.
It is provided by the invention asymmetric based on the big steric hindrance that 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone is skeleton (alpha-diimine) nickel alkene catalyst, shown in general structure such as formula (I):
In formula (I), R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl or Methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups, R4For Methyl, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl, X is chlorine or bromine.Formula (I) selection of all aniline substituent groups is independent from each other in.
Preferably, formula (I) R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl or bis- (4- fluorobenzene Base) methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen or methoxyl groups, R4For methyl, Ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen or methyl, X is bromine.
Shown in catalyst ligand general structure provided by the invention such as formula (II):
In formula (II), R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl Or methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups, R4 For methyl, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl.Institute in formula (II) There is the selection of aniline substituent group to be independent from each other.
Preferably, formula (II) R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl or bis- (4- fluorine Phenyl) methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen or methoxyl groups, R4For first Base, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen or methyl.
It is furthermore preferred that any one of ligand in compound as shown in table 1 shown in above-mentioned (II):
1 ligand of table
The present invention also provides a kind of methods for preparing above-mentioned ligand compound, and it includes following steps:
1), 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone is contracted with the aniline with big steric hindrance substituent group by ketoamine It closes reaction and obtains compound shown in formula (III):
The aniline substituent group that step reaction uses can refer to table 1;Toluene can be used in the solvent that step reaction uses, and will have The aniline of big steric hindrance substituent group is reacted with trimethyl aluminium generates aluminum amine salt, then aluminum amine salt and phenanthrenequione are carried out ketoamine condensation reaction. The mixed solvent or petroleum ether of product methylene chloride and petroleum ether and the mixed solvent of ethyl acetate are eluent in silica gel Column chromatography is carried out in column, obtains product shown in formula (III).
2), compound shown in formula (III) obtains formula (II) by ketoamine condensation reaction with the aniline with small steric hindrance substituent group Corresponding compound:
The aniline substituent group that step reaction uses can refer to table 1;The step reaction use solvent can be selected from toluene, acetonitrile, At least one of acetic acid and dehydrated alcohol, preferably toluene and acetonitrile;The catalyst that step reaction uses is selected from p-methyl benzenesulfonic acid At least one of with acetic acid;The use of compound shown in the catalyst, formula (III), the aniline with small steric hindrance substituent group and solvent Amount is than being 0.2-0.5mmol:1-1.1mmol:1.1-1.4mmol:30-70ml, preferably 0.3mmol:1mmol:1.1mmol: 50ml, the step reaction time are 6-16 hours, preferably 8-12 hours.The mixed solvent or stone of product methylene chloride and petroleum ether The mixed solvent of oily ether and ethyl acetate is eluent in silicagel column progress column chromatography, obtains product shown in formula (II).
The present invention also provides a kind of preparation methods of catalyst shown in formula (I) comprising the steps of: in atmosphere of inert gases Under, by compound shown in formula (II) and glycol dimethyl ether Nickel Bromide, glycol dimethyl ether Nickel Chloride or six hydration dichloros Change one of nickel to be complexed, catalyst of the present invention can be obtained.X in catalyst structure formula of the present invention be chlorine or Bromine selects X for bromine for polymerization effect without substantial effect in the embodiment of the present invention.
Preferably, under nitrogen atmosphere, compound shown in formula (II) can be selected from ligand shown in table 1, with containing for ligand complex Nickel compound selects glycol dimethyl ether Nickel Bromide (DME) NiBr2, the ligand and (DME) NiBr2Molar ratio be 1:1- 1.2, preferably 1:1.1;The solvent be methylene chloride, reaction temperature be 15-35 DEG C, preferably 25 DEG C, reaction time 8-30 hour, It is preferred that 24 hours.When X is bromine, referring to the ligand scheme of table 1, catalyst of the invention can be selected from any one in table 2:
2 catalyst of table
The present invention also provides a kind of carbon monoxide-olefin polymerics for catalysis in olefine polymerization, and the composition is by shown in formula (I) Catalyst and co-catalyst form, and the co-catalyst is selected from least one of chlorination alkyl aluminum, alkyl aluminum and aikyiaiurnirsoxan beta, institute Stating alkene is ethylene or propylene.
In above-mentioned carbon monoxide-olefin polymeric, the aikyiaiurnirsoxan beta be methylaluminoxane (MAO), modified methylaluminoxane (MMAO), Ethylaluminoxane or isobutyl aluminium alkoxide;The alkyl aluminum is trimethyl aluminium, triethyl aluminum, triisobutyl aluminium, tri-n-hexyl aluminum Or tri-n-octylaluminium;The chlorination alkyl aluminum is diethylaluminum chloride, sesquialter aluminium diethyl monochloride or ethylaluminium dichloride;From helping The using effect and cost consideration of catalyst, preferably chlorination alkyl aluminum as co-catalyst, metallic aluminium in chlorination alkyl aluminum with The molar ratio abbreviation aluminium nickel ratio of metallic nickel in catalyst, aluminium nickel than range be 50-1000:1, preferably 100-800:1, more preferably 200-600:1, more preferable 400:1.
The invention also discloses the catalyst as shown in formula (I) in catalysis ethylene, propylene polymerization, prepares polyethylene, polypropylene In application.
The beneficial effects of the present invention are provide a kind of (Asia α-two with good thermal stability and polymerization activity Amine) nickel olefin polymerization catalyst.
Specific embodiment
The present invention is further elaborated combined with specific embodiments below, but the present invention is not limited to following embodiments.
Be specifically related in the embodiment of the present invention such as chemical structural formula (I), (II), (III) compound represented such as 3 institute of table Show:
Table 3
Embodiment 1, preparation A1: in the toluene of (the benzhydryl) -4- methylaniline of 2,6- bis- (8.8g, 20mmol) The toluene solution 20ml (1.0M, 20mmol) of trimethyl aluminium is added in (100mL) solution, is reacted 2 hours at 120 DEG C, it will be anti- It answers temperature to be down to room temperature, 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone (4.2g, 18mmol) is then added, heats up back Stream reaction for 24 hours, is cooled to room temperature, and is terminated with 5% sodium hydrate aqueous solution.Organic phase is extracted with ethyl acetate, and then uses nothing Aqueous sodium persulfate is dry, removal solvent, and the mixed solvent that the volume ratio of residue methylene chloride and petroleum ether is 2:1 carries out silica gel Column chromatography, the quality for obtaining A1 is 5.0g, yield: 38%.
Embodiment 2, preparation A2: in the toluene of (the benzhydryl) -6- methylaniline of 2,4- bis- (8.8g, 20mmol) The toluene solution 20ml (1.0M, 20mmol) of trimethyl aluminium is added in (100mL) solution, is reacted 2 hours at 120 DEG C, it will be anti- It answers temperature to be down to room temperature, 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone (4.2g, 18mmol) is then added, heats up back Stream reaction for 24 hours, is cooled to room temperature, and is terminated with 5% sodium hydrate aqueous solution.Organic phase is extracted with ethyl acetate, and then uses nothing Aqueous sodium persulfate is dry, removal solvent, and the mixed solvent that the volume ratio of residue methylene chloride and petroleum ether is 2:1 carries out silica gel Column chromatography, the quality for obtaining A2 is 5.4g, yield: 41%.
Embodiment 3, preparation A3: in bis- (bis- (4- fluorophenyl) methyl) -4- methylanilines (10.2g, 20mmol) of 2,6- The toluene solution 20ml (1.0M, 20mmol) of trimethyl aluminium is added in toluene (100mL) solution, is reacted 2 hours at 120 DEG C, Reaction temperature is down to room temperature, 9,10- dihydro -9,10- ethylene anthracene -11,12- diketone (4.2g, 18mmol) is then added, is heated up Back flow reaction for 24 hours, is cooled to room temperature, and is terminated with 5% sodium hydrate aqueous solution.Organic phase is extracted with ethyl acetate, and then uses Anhydrous sodium sulfate is dry, removal solvent, and the mixed solvent that the volume ratio of residue methylene chloride and petroleum ether is 2:1 carries out silicon Plastic column chromatography, the quality for obtaining A3 is 5.8g, yield: 40%.
Embodiment 4, preparation L1: at 2,6- dimethylaniline (0.133g, 1.1mmol) and A1 (0.656g, 1mmol) P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in toluene (50ml) solution, back flow reaction 12h.Solvent is removed, residue is used The mixed solvent that the volume ratio of petroleum ether and ethyl acetate is 30:1 carries out silica gel column chromatography, and the quality for obtaining L1 is 0.4g, produces Rate: 53%.
Embodiment 5, preparation L2: at 2,6- diethylaniline (0.164g, 1.1mmol) and A1 (0.656g, 1mmol) P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in toluene (50ml) solution, back flow reaction 12h.Solvent is removed, residue is used The mixed solvent that the volume ratio of petroleum ether and ethyl acetate is 30:1 carries out silica gel column chromatography, and the quality for obtaining L2 is 0.43g, produces Rate: 55%.
Embodiment 6, preparation L3: in 2,6-DIPA (0.195g, 1.1mmol) and A1 (0.656g, 1mmol) Toluene (50ml) solution in be added p-methyl benzenesulfonic acid (0.086g, 0.5mmol), back flow reaction 12h.Remove solvent, residue The mixed solvent that volume ratio with petroleum ether and ethyl acetate is 30:1 carries out silica gel column chromatography, and the quality for obtaining L3 is 0.42g, Yield: 52%.
Embodiment 7, preparation L12: 2,6- diethyl -4- methylaniline (0.179g, 1.1mmol) and A2 (0.656g, P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in toluene (50ml) solution 1mmol), back flow reaction 12h.Solvent is removed, The mixed solvent that the volume ratio of residue petroleum ether and ethyl acetate is 30:1 carries out silica gel column chromatography, obtains the quality of L12 For 0.45g, yield: 56%.
Embodiment 8, preparation L20: 2,6- diethyl -4- methylaniline (0.179g, 1.1mmol) and A3 (0.728g, P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in toluene (50ml) solution 1mmol), back flow reaction 12h.Solvent is removed, The mixed solvent that the volume ratio of residue petroleum ether and ethyl acetate is 30:1 carries out silica gel column chromatography, obtains the quality of L20 For 0.48g, yield: 55%.
Embodiment 9, preparation C1: under nitrogen atmosphere, by L1 (0.152g, 0.2mmol) and (DME) NiBr2(0.062g, It 0.2mmol) is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, wash 3 times with ether, often Secondary ether dosage is 20ml, then ether is drained to obtain solid C1,0.176g, yield 90%.
Embodiment 10, preparation C2: under nitrogen atmosphere, by L2 (0.157g, 0.2mmol) and (DME) NiBr2 (0.062g, 0.2mmol) is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, is washed with ether It washs 3 times, each ether dosage is 20ml, then ether is drained to obtain solid C2,0.177g, yield 88%.
Embodiment 11, preparation C3: under nitrogen atmosphere, by L3 (0.163g, 0.2mmol) and (DME) NiBr2 (0.062g, 0.2mmol) is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, is washed with ether It washs 3 times, each ether dosage is 20ml, then ether is drained to obtain solid C3,0.184g, yield 89%.
Embodiment 12, preparation C12: under nitrogen atmosphere, by L12 (0.160g, 0.2mmol) and (DME) NiBr2 (0.062g, 0.2mmol) is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, is washed with ether It washs 3 times, each ether dosage is 20ml, then ether is drained to obtain solid C12,0.185g, yield 91%.
Embodiment 13, preparation C20: under nitrogen atmosphere, by L20 (0.175g, 0.2mmol) and (DME) NiBr2 (0.062g, 0.2mmol) is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, is washed with ether It washs 3 times, each ether dosage is 20ml, then ether is drained to obtain solid C20,0.192g, yield 88%.
Following embodiment is catalyzed ethylene polymerization:
Embodiment 14, ethylene pressure polymerization are carried out under the conditions of anhydrous and oxygen-free.Ethylene pressure is 1MPa, polymerization temperature It is 60 DEG C, 1L heptane is imported in the stainless steel cauldron of 2000mL, then injection 2.5ml concentration is 2.0mol/L thereto Co-catalyst diethylaluminum chloride toluene solution.10 μm of ol major catalyst C1 are dissolved with 10mL toluene solution, are injected into, it will Ethylene is forced into 1MPa, and polymer solution is poured into the ethanol solution of acidification and settled after reacting half an hour by stirring, mistake Polymer is filtered, is then washed for several times with acidic ethanol, weighs to obtain 24.3g polymer after constant weight is dried under vacuum at 60 DEG C.It urges Changing activity is 4.86 × 106gPE[mol(Ni)h]-1
C1 in embodiment 14 is replaced with C2 by embodiment 15, and other conditions are constant, by polymerizate at 60 DEG C vacuum 25.8g polymer is weighed to obtain after drying to constant weight.Catalytic activity is 5.16 × 106gPE[mol(Ni)h]-1
C1 in embodiment 14 is replaced with C3 by embodiment 16, and polymerization temperature is set as 20 DEG C, and other conditions are constant, will be gathered It closes after product is dried under vacuum to constant weight at 60 DEG C and weighs to obtain 53.1g polymer.Catalytic activity is 10.6 × 106gPE[mol (Ni)h]-1
C1 in embodiment 14 is replaced with C12 by embodiment 17, and it is 3.0mol/L's that co-catalyst, which is changed to 10ml concentration, MAO toluene solution, other conditions are constant, and polymerizate is dried under vacuum to after constant weight at 60 DEG C and weighs to obtain 18.9g polymer. Catalytic activity is 3.78 × 106gPE[mol(Ni)h]-1
C1 in embodiment 14 is replaced with C20 by embodiment 18, and other conditions are constant, and polymerizate is true at 60 DEG C 22.9g polymer is weighed to obtain after sky drying to constant weight.Catalytic activity is 4.58 × 106gPE[mol(Ni)h]-1
Polymerization temperature in embodiment 18 is adjusted to 70 DEG C by embodiment 19, and other conditions are constant, by polymerizate 60 15.8g polymer is weighed to obtain after being dried under vacuum to constant weight at DEG C.Catalytic activity is 3.16 × 106gPE[mol(Ni)h]-1

Claims (8)

1. (alpha-diimine) Raney nickel shown in formula (I):
In formula (I), R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl or first Base, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups, R4For first Base, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl, X is chlorine or bromine.
2. catalyst according to claim 1, it is characterised in that: the R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl or bis- (4- fluorophenyl) methyl, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, Halogen or methoxyl group, R4For methyl, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen or methyl, X is bromine.
3. compound shown in formula (II):
In formula (II), R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl or first Base, R3For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups, R4For first Base, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl.
, 9,10- 4. a kind of method for preparing the corresponding compound of formula as claimed in claim 3 (II), it includes following steps: 1) Dihydro -9,10- ethylene anthracene -11,12- diketone obtains formula (III) by ketoamine condensation reaction with the aniline with big steric hindrance substituent group Shown compound:
Wherein R1For benzhydryl or bis- (4- fluorophenyl) methyl, R2For benzhydryl, bis- (4- fluorophenyl) methyl or methyl, R3 For methyl, ethyl, isopropyl, benzhydryl, bis- (4- fluorophenyl) methyl, halogen, trifluoromethyl or methoxyl groups;
2), it is corresponding with the aniline with small steric hindrance substituent group by ketoamine condensation reaction to obtain formula (II) for compound shown in formula (III) Compound:
Wherein R4For methyl, ethyl or isopropyl, R5For methyl, ethyl or isopropyl, R6For hydrogen, methyl, ethyl or isopropyl.
5. a kind of method for preparing catalyst as claimed in claim 1 or 2 comprising the steps of: under atmosphere of inert gases, will weigh Benefit requires 3 compounds and glycol dimethyl ether Nickel Bromide, glycol dimethyl ether Nickel Chloride or six hydration Nickel Chlorides One of be complexed, catalyst of any of claims 1 or 2 can be obtained.
6. a kind of carbon monoxide-olefin polymeric for catalysis in olefine polymerization, which is characterized in that include master of any of claims 1 or 2 Catalyst and co-catalyst, wherein the co-catalyst is selected from least one of chlorination alkyl aluminum, alkyl aluminum and aikyiaiurnirsoxan beta, The alkene is ethylene or propylene.
7. a kind of polyethylene, which is characterized in that the polyethylene is catalyzed ethylene by carbon monoxide-olefin polymeric as claimed in claim 6 Polymerization obtains.
8. a kind of polypropylene, which is characterized in that the polypropylene is catalyzed propylene by carbon monoxide-olefin polymeric as claimed in claim 6 Polymerization obtains.
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CN110483586A (en) * 2019-08-27 2019-11-22 中国科学技术大学 Big steric hindrance ketimide Raney nickel and its ligand compound, preparation method and application
CN110511251A (en) * 2019-08-20 2019-11-29 中山大学 A kind of alpha-nickel diimine compound, metallic catalyst, branched polyethylene wax and its preparation method and application
CN112745360A (en) * 2019-10-31 2021-05-04 中国石油化工股份有限公司 Amino imine complex and preparation method and application thereof
CN115246896A (en) * 2021-04-28 2022-10-28 中国石油化工股份有限公司 Double/multi-metal catalyst and preparation method and application thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104926962A (en) * 2015-05-15 2015-09-23 浙江大学 Ethylene acenaphthylene (alpha-diimine) nickel complex/alkyl aluminum chloride combined catalyst
CN105294778A (en) * 2015-10-14 2016-02-03 中山大学 Nickel base complex, and preparation method and application thereof
CN105481998A (en) * 2014-09-18 2016-04-13 中国石油化工股份有限公司 Olefin polymerization catalyst as well as preparation method and application method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105481998A (en) * 2014-09-18 2016-04-13 中国石油化工股份有限公司 Olefin polymerization catalyst as well as preparation method and application method thereof
CN104926962A (en) * 2015-05-15 2015-09-23 浙江大学 Ethylene acenaphthylene (alpha-diimine) nickel complex/alkyl aluminum chloride combined catalyst
CN105294778A (en) * 2015-10-14 2016-02-03 中山大学 Nickel base complex, and preparation method and application thereof

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
HAO LIU ET AL: "2,6-Dibenzhydryl-N-(2-phenyliminoacenaphthylenylidene)-4-methylbenzenamine Nickel Dibromides:Synthesis,Characterization,and Ethylene Polymerization", 《ORGANOMETALLICS》 *
傅智盛等: "α-二亚胺配体的研究进展", 《合成树脂及塑料》 *
王俊: "用于乙烯聚合的镍配合物催化剂的研究进展", 《石油化工(石油加工)》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110511251A (en) * 2019-08-20 2019-11-29 中山大学 A kind of alpha-nickel diimine compound, metallic catalyst, branched polyethylene wax and its preparation method and application
CN110483586A (en) * 2019-08-27 2019-11-22 中国科学技术大学 Big steric hindrance ketimide Raney nickel and its ligand compound, preparation method and application
CN112745360A (en) * 2019-10-31 2021-05-04 中国石油化工股份有限公司 Amino imine complex and preparation method and application thereof
CN112745360B (en) * 2019-10-31 2022-10-21 中国石油化工股份有限公司 Amino imine complex and preparation method and application thereof
CN115246896A (en) * 2021-04-28 2022-10-28 中国石油化工股份有限公司 Double/multi-metal catalyst and preparation method and application thereof
CN115246896B (en) * 2021-04-28 2023-08-15 中国石油化工股份有限公司 Double/multi-metal catalyst and preparation method and application thereof

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