CN109957050A - 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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CN109957050A
CN109957050A CN201811560455.3A CN201811560455A CN109957050A CN 109957050 A CN109957050 A CN 109957050A CN 201811560455 A CN201811560455 A CN 201811560455A CN 109957050 A CN109957050 A CN 109957050A
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methyl
isopropyl
ethyl
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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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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 1,2- benzo acenaphthenequinone is skeleton.Structural formula such as formula (I) based on asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance that 1,2- benzo acenaphthenequinone is skeleton of the invention is shown, 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 preparation process of the catalyst 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 more particularly to one Kind is based on asymmetric (alpha-diimine) nickel alkene catalyst of big steric hindrance and preparation method thereof that 1,2- benzo acenaphthenequinone is skeleton, and makes Polyethylene or polyacrylic application are obtained with the catalyst ethylene or propylene.
Background technique
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:
The purpose of the present invention is overcome the deficiencies of the prior art and provide a kind of big position based on 1,2- benzo acenaphthenequinone for skeleton Hinder asymmetric (alpha-diimine) nickel alkene catalyst and its preparation method and application.
Asymmetry (alpha-diimine) nickel alkene catalyst provided by the invention, shown in general formula of the chemical 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, R described in formula (II)1For 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 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), 1,2- benzo acenaphthenequinone is obtained shown in formula (III) with the aniline with big steric hindrance substituent group by ketoamine condensation reaction 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 catalyst, 1,2- benzo acenaphthenequinone, the aniline with big steric hindrance substituent group and solvent amount ratio For 0.1-0.15mmol:1-1.1mmol:1.1-1.4mmol:5-10ml, preferably 0.1mmol:1mmol:1.1mmol:8ml; The step reaction time is 2-8 hours, preferably 3-6 hours.The mixed solvent or petroleum ether of product methylene chloride and petroleum ether Mixed solvent with ethyl acetate is that eluent carries out column chromatography in silicagel column, obtains the product as 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 solvent that step reaction uses is selected from toluene, acetonitrile, second At least one of acid and dehydrated alcohol, preferably toluene and acetonitrile;The step reaction use catalyst be selected from p-methyl benzenesulfonic acid and At least one of acetic acid;The dosage of compound shown in the catalyst, formula (III), the aniline with small steric hindrance substituent group and solvent Than for 0.2-0.5mmol:1-1.1mmol:1.1-1.4mmol:30-70ml, preferably 0.3mmol:1mmol:1.1mmol: 50ml;The step reaction time is 6-16 hours, preferably 8-12 hours.The mixed solvent of product methylene chloride and petroleum ether or The mixed solvent of petroleum 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 16-24 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 Kind:
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 invention has the advantages that being matched under the premise of unobvious increase side group substituent group steric hindrance by improving Frame structure provides a kind of with the catalysis of (alpha-diimine) nickel olefin polymerization of good thermal stability and polymerization activity Agent.
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
Prepare A1: in (the benzhydryl) -4- methylaniline of 2,6- bis- (8.8g, 20mmol) and 1,2- benzo acenaphthenequinone (4.2g, P-methyl benzenesulfonic acid (0.34g, 2mmol) is added in toluene (150mL) solution 18mmol), back flow reaction 6h.Solvent is removed, is remained The mixed solvent that the volume ratio of excess methylene chloride and petroleum ether is 2:1 carries out silica gel column chromatography, and the quality for obtaining A1 is 4.1g, yield: 35%.
Embodiment 2
Prepare A2: in (the benzhydryl) -6- methylaniline of 2,4- bis- (8.8g, 20mmol) and 1,2- benzo acenaphthenequinone (4.2g, P-methyl benzenesulfonic acid (0.34g, 2mmol) is added in toluene (150mL) solution 18mmol), back flow reaction 6h.Solvent is removed, is remained The mixed solvent that the volume ratio of excess methylene chloride and petroleum ether is 2:1 carries out silica gel column chromatography, and the quality for obtaining A2 is 5.0g, yield: 42%.
Embodiment 3
Prepare A3: in bis- (bis- (4- fluorophenyl) methyl) -6- methylanilines (10.2g, 20mmol) and 1 of 2,4-, 2- benzo P-methyl benzenesulfonic acid (0.34g, 2mmol) is added in toluene (150mL) solution of acenaphthenequinone (4.2g, 18mmol), back flow reaction 10h. The mixed solvent that the volume ratio of removal solvent, residue methylene chloride and petroleum ether is 2:1 carries out silica gel column chromatography, obtains A3 Quality be 6.3g, yield: 48%.
Embodiment 4
Prepare L1: in the toluene (50ml) of 2,6- dimethylaniline (0.133g, 1.1mmol) and A1 (0.653g, 1mmol) P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in solution, back flow reaction 12h.Remove solvent, residue petroleum ether and second The mixed solvent that the volume ratio of acetoacetic ester is 30:1 carries out silica gel column chromatography, and the quality for obtaining L1 is 0.31g, yield: 41%.
Embodiment 5
Prepare L2: in the toluene (50ml) of 2,6- diethylaniline (0.164g, 1.1mmol) and A1 (0.653g, 1mmol) P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in solution, back flow reaction 12h.Remove solvent, residue petroleum ether and second The mixed solvent that the volume ratio of acetoacetic ester is 30:1 carries out silica gel column chromatography, and the quality for obtaining L2 is 0.28g, yield: 36%.
Embodiment 6
Prepare L3: in the toluene of 2,6-DIPA (0.195g, 1.1mmol) and A1 (0.653g, 1mmol) P-methyl benzenesulfonic acid (0.086g, 0.5mmol) is added in (50ml) solution, back flow reaction 12h.Remove solvent, residue petroleum The volume ratio of ether and ethyl acetate be 30:1 mixed solvent carry out silica gel column chromatography, obtain L3 quality be 0.33g, yield: 41%.
Embodiment 7
Prepare L12: in 2,6- diethyl -4- methylaniline (0.179g, 1.1mmol) and A2 (0.653g, 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 L12 is 0.31g, Yield: 39%.
Embodiment 8
Prepare L20: in 2,6- diethyl -4- methylaniline (0.179g, 1.1mmol) and A3 (0.725g, 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 L20 is 0.37g, Yield: 43%.
Embodiment 9
Prepare C1: under nitrogen atmosphere, by L1 (0.151g, 0.2mmol) and (DME) NiBr2(0.062g,0.2mmol) It is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, washed 3 times with ether, each ether Dosage is 20ml, then ether is drained to obtain solid C1,0.171g, yield 88%.
Embodiment 10
Prepare C2: under nitrogen atmosphere, by L2 (0.156g, 0.2mmol) and (DME) NiBr2(0.062g,0.2mmol) It is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, washed 3 times with ether, each ether Dosage is 20ml, then ether is drained to obtain solid C2,0.172g, yield 86%.
Embodiment 11
Prepare C3: under nitrogen atmosphere, by L3 (0.162g, 0.2mmol) and (DME) NiBr2(0.062g,0.2mmol) It is dissolved in 20ml methylene chloride, is stirred at room temperature 24 hours, methylene chloride is drained, washed 3 times with ether, each ether Dosage is 20ml, then ether is drained to obtain solid C3,0.188g, yield 89%.
Embodiment 12
Prepare C12: under nitrogen atmosphere, by L12 (0.160g, 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 C12,0.186g, yield 90%.
Embodiment 13
Prepare C20: under nitrogen atmosphere, by L20 (0.174g, 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 C20,0.191g, yield 88%.
Following embodiment is catalyzed ethylene polymerization:
Embodiment 14
Ethylene pressure polymerization is carried out under the conditions of anhydrous and oxygen-free.Ethylene pressure is 1MPa, and polymerization temperature is 60 DEG C, will 1L heptane imports in the stainless steel cauldron of 2000mL, the co-catalyst that then injection 2.5ml concentration is 2.0 mol/L thereto Diethylaluminum chloride toluene solution.10 μm of ol major catalyst C1 are dissolved with 10mL toluene solution, is injected into, ethylene is forced into Polymer solution is poured into the ethanol solution of acidification and is settled after reacting half an hour by 1MPa, stirring, filtered polymeric, so It is washed for several times with acidic ethanol afterwards, weighs to obtain 24.3g polymer after constant weight is dried under vacuum at 60 DEG C.Catalytic activity is 4.86×106gPE[mol(Ni)h] -1, polymerizate weight average molecular weight is 33.6 × 104G/mol, polydispersity coefficient 2.17.
Embodiment 15
C1 in embodiment 14 is replaced with into C2, other conditions are constant, and polymerizate is dried under vacuum to perseverance at 60 DEG C 25.8g polymer is weighed to obtain after weight.Catalytic activity is 5.16 × 106gPE[mol(Ni)h]-1, polymerizate weight average molecular weight is 37.2×104G/mol, polydispersity coefficient 2.31.
Embodiment 16
C1 in embodiment 14 is replaced with into C3, polymerization temperature is set as 20 DEG C, and other conditions are constant, by polymerizate 60 53.1g polymer is weighed to obtain after being dried under vacuum to constant weight at DEG C.Catalytic activity is 10.6 × 106gPE[mol(Ni)h]-1, polymerization Product weight average molecular weight is 104.3 × 104G/mol, polydispersity coefficient 2.35.
Embodiment 17
C1 in embodiment 14 is replaced with into C12, polymerization temperature is set as 80 DEG C, and co-catalyst is changed to 10ml concentration and is The MMAO toluene solution of 3.0mol/L, other conditions are constant, weigh after polymerizate is dried under vacuum to constant weight at 60 DEG C 18.9g polymer.Catalytic activity is 3.78 × 106gPE[mol(Ni)h]-1
Embodiment 18
C1 in embodiment 14 is replaced with into C20, other conditions are constant, and polymerizate is dried under vacuum to perseverance at 60 DEG C 22.9g polymer is weighed to obtain after weight.Catalytic activity is 4.58 × 106gPE[mol(Ni)h]-1, polymerizate weight average molecular weight is 13.3×104G/mol, polydispersity coefficient 2.56.
Embodiment 19
Polymerization temperature in embodiment 18 is adjusted to 70 DEG C, other conditions are constant, by polymerizate at 60 DEG C vacuum 15.8g polymer is weighed to obtain after drying to constant weight.Catalytic activity is 3.16 × 106gPE[mol(Ni)h]-1, polymerizate weighs equal Molecular weight is 11.6 × 104G/mol, polydispersity coefficient 2.53.
Comparative example 1
1,2- benzo acenaphthenequinone in embodiment 1 is replaced with to the acenaphthenequinone of same molar, prepares (2,6- bis- (hexichol first Base) -4- methylaniline) acenaphthene ketone, code name D1, yield: 32%.
Comparative example 2
A1 in embodiment 5 is replaced with to the D1 of same molar, prepares 1- (2,6- diethylaniline) -2- (2,6- bis- (benzhydryl) -4- methylaniline) acenaphthene, code name E1, yield 34%.
Comparative example 3
L2 in embodiment 10 is replaced with to the E1 of same molar, prepares (1- (2,6- diethylaniline) -2- (2,6- Two (benzhydryl) -4- methylanilines) acenaphthene) close nickelous bromide, code name F1, yield 85%.
Comparative example 4
C2 in embodiment 15 is replaced with to the F1 of same molar, other conditions are constant, polymerization catalytic activity 4.26 ×106gPE[mol(Ni)h]-1, polymerizate weight average molecular weight is 31.2 × 104G/mol, polydispersity coefficient 2.27.
Comparative example 5
1,2- benzo acenaphthenequinone in embodiment 3 is replaced with to the acenaphthenequinone of same molar, prepares (2,4- bis- (bis- (4- fluorobenzene Base) methyl) -6- methylaniline) acenaphthene ketone, code name D2, yield: 51%.
Comparative example 6
A3 in embodiment 8 is replaced with to the D2 of same molar, prepares 1- (2,6- diethyl -4- methylaniline) -2- (2,4- bis- (bis- (4- fluorophenyl) methyl) -6- methylaniline) acenaphthene, code name E2, yield 46%.
Comparative example 7
L20 in embodiment 13 is replaced with to the E2 of same molar, prepares (1- (2,6- diethyl -4- methylaniline) - 2- (2,4- bis- (bis- (4- fluorophenyl) methyl) -6- methylaniline) acenaphthene) close nickelous bromide, code name F2, yield 83%.
Comparative example 8
C20 in embodiment 19 is replaced with to the F2 of same molar, other conditions are constant, and polymerization catalytic activity is 2.41×106gPE[mol(Ni)h]-1, polymerizate weight average molecular weight is 9.6 × 104G/mol, polydispersity coefficient 2.33.

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.
4. a kind of method for preparing the corresponding compound of formula described in claim 3 (II), it includes following steps:
1), 1,2- benzo acenaphthenequinone obtains chemical combination shown in formula (III) by ketoamine condensation reaction with the aniline with big steric hindrance substituent group Object:
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), compound shown in formula (III) obtains the formula (II) by ketoamine condensation reaction with the aniline with small steric hindrance substituent group Corresponding 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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