Ethylene-hydroxyl-containing alpha-olefin copolymer and preparation method thereof

Abstract

The invention relates to the field of olefin polymerization, and discloses an ethylene-hydroxyl-containing alpha-olefin copolymer and a preparation method thereof. The preparation method of the ethylene-hydroxyl-containing alpha-olefin copolymer provided by the invention comprises the following steps: ethylene and hydroxyl-containing alpha-olefin are subjected to a copolymerization reaction by using a catalyst composition, and the catalyst composition comprises the following components: a) a transition metal compound; and b) a co-catalyst component. The preparation method of the ethylene-hydroxyl-containing alpha-olefin copolymer has the advantages that the catalytic activity and the comonomer insertion rate are improved.

Description

Technical Field

[0001] The invention relates to the field of olefin polymerization, and in particular to an ethylene-hydroxyl-containing alpha-olefin copolymer and a preparation method thereof. Background Art

[0002] Single-site catalysts for olefin polymerization have been a research hotspot in organometallic chemistry, catalysis, polymer chemistry, and materials science in recent decades. Using this type of catalyst, olefin polymers with uniform molecular weight distribution and chemical composition distribution can be obtained, and the molecular structure and molecular weight of the polymer can be highly controllable by adjusting the catalyst structure. Since this type of catalyst is highly efficient and broad-spectrum when applied to olefin copolymerization (ChemistrySelect 2020, 5, 7581-7585), olefin polymers that cannot be obtained with traditional Ziegler-Natta catalysts can be obtained by using this type of catalyst.

[0003] Non-metallocene transition metal catalysts are important components of single-site catalysts. They have rich ligand structures and simple synthesis processes. Their catalytic performance can be easily adjusted by adjusting the ligand structure (Chemical Reviews, 2003, 103, 283-315).

[0004] Polyolefin materials containing polar groups have superior properties. They not only have the excellent mechanical, optical, processing and other properties of traditional polyolefin materials, but also have greatly improved surface properties such as dyeability, wettability, adhesion, etc. due to the introduction of polar groups. At the same time, they may have improved compatibility with other polar polymer materials and have good application prospects.

[0005] The catalysts used in the prior art are not yet sufficiently high in catalytic activity and comonomer insertion rate, and there is room for further improvement. Summary of the invention

[0006] The object of the present invention is to provide a novel method for preparing an ethylene-hydroxyl-containing α-olefin copolymer and the prepared ethylene-hydroxyl-containing α-olefin copolymer. The method for preparing an ethylene-hydroxyl-containing α-olefin copolymer according to the present invention has the advantages of improving catalytic activity and comonomer insertion rate.

[0007] In order to achieve the above object, the present invention provides a method for preparing an ethylene-hydroxyl-containing α-olefin copolymer, wherein the method comprises: using a catalyst composition to copolymerize ethylene and a hydroxyl-containing α-olefin,

[0008] Wherein, the catalyst composition comprises the following components:

[0009] a) a transition metal compound having a structure represented by formula (1);

[0010] b) a co-catalyst component,

[0011]

[0012] In formula (1), M is a tetravalent transition metal atom; X and Y are each independently a hydrocarbonoxy group having 1 to 10 carbon atoms or a halogen.

[0013] Preferably, M is a titanium atom, a zirconium atom or a hafnium atom, more preferably a titanium atom or a zirconium atom.

[0014] Preferably, X and Y are each independently a hydrocarbonoxy group having 1 to 6 carbon atoms, a fluorine atom, a chlorine atom, a bromine atom or an iodine atom; more preferably, X and Y are each independently a hydrocarbonoxy group having 1 to 3 carbon atoms or a chlorine atom.

[0015] Preferably, the alkoxy group having 1 to 10 carbon atoms is methoxy, ethoxy, propoxy or isopropoxy.

[0016] Preferably, X and Y are both isopropoxy or ethoxy; or, X and Y are both chlorine atoms.

[0017] Preferably, the co-catalyst component comprises an alkylaluminoxane, a combination of an organoboron compound and an organoaluminum compound, or a combination of an organoaluminum compound and an organomagnesium compound; more preferably, the co-catalyst component is an alkylaluminoxane, a combination of an organoboron compound and an organoaluminum compound, or a combination of an organoaluminum compound and an organomagnesium compound.

[0018] Preferably, the alkylaluminoxane is a compound selected from the structure represented by formula (2) and / or formula (3),

[0019]

[0020] In formula (2) and formula (3), R is selected from an alkyl group having 1 to 15 carbon atoms, and n represents an integer of 4 to 30; more preferably, R is selected from an alkyl group having 1 to 5 carbon atoms, and n represents an integer of 10 to 30; further preferably, the alkylaluminoxane is methylaluminoxane.

[0021] Preferably, the organic boron compound is one or more of triphenylmethyl tetrakis(pentafluorophenyl)borate, N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate and tris(pentafluorophenyl)boron.

[0022] Preferably, the organoaluminum compound is a compound having a structure represented by the general formula AlX1X2X3, wherein X1, X2 and X3 are respectively a halogen atom, an alkyl group having 1-8 carbon atoms, an alkoxy group having 1-8 carbon atoms, and an aryloxy group having 6-12 carbon atoms, X1, X2 and X3 may be the same or different, and at least one is an alkyl group having 1-8 carbon atoms; more preferably, the organoaluminum compound is triisobutylaluminum.

[0023] Preferably, the organic magnesium compound is an organic magnesium compound containing two alkyl groups with carbon atoms of 1-10, preferably an organic magnesium compound containing two alkyl groups with carbon atoms of 1-6, and more preferably di-n-butyl magnesium.

[0024] Preferably, the co-catalyst component is alkylaluminoxane, and the molar ratio of the transition metal compound to the alkylaluminoxane calculated as aluminum is 1:(100-20000), preferably 1:(200-10000), and more preferably 1:(500-5000).

[0025] Preferably, the co-catalyst component is a combination of an organic boron compound and an organic aluminum compound, the molar ratio of the transition metal compound to the organic boron compound is 1:(1-5), preferably 1:(1-2), and the molar ratio of the transition metal compound to the organic aluminum compound is 1:(10-5000), preferably 1:(50-1000), and more preferably 1:(100-500).

[0026] Preferably, the co-catalyst component is a combination of an organic aluminum compound and an organic magnesium compound, the molar ratio of the transition metal compound to the organic aluminum compound is 1:(30-5000), preferably 1:(100-1000), more preferably 1:(100-500), and the molar ratio of the transition metal compound to the organic magnesium compound is 1:(10-2000), preferably 1:(100-1000).

[0027] Preferably, the molar ratio of the organoaluminum compound to the organomagnesium compound is greater than 2.5:1.

[0028] Preferably, the hydroxyl-containing α-olefin is reacted with an alkyl aluminum before use. The alkyl aluminum is an aluminum compound containing three alkyl groups with carbon atoms of 2 to 8, preferably triethyl aluminum and triisobutyl aluminum.

[0029] Preferably, the molar ratio of the alkyl aluminum to the hydroxyl-containing α-olefin is 1.0-2.0:1, preferably 1.0-1.2:1.

[0030] Preferably, the concentration of the transition metal compound in the copolymerization reaction system is 1×10 -10 mol / L~1×10-3 mol / L, preferably 1×10 -8 mol / L~1×10 -5 mol / L.

[0031] Preferably, the copolymerization temperature is -50 to 200° C., and the copolymerization time is 1 to 300 minutes.

[0032] Preferably, the copolymerization reaction temperature is -20 to 150° C., and the copolymerization reaction time is 5 to 60 minutes.

[0033] Preferably, the hydroxyl-containing α-olefin is a terminal olefin containing 3 to 18 carbon atoms and containing one or more hydroxyl groups, preferably allyl alcohol, 3-butene-1-ol, 4-pentene-1-ol, 4-pentene-2-ol, 5-hexene-1-ol, 6-heptene-1-ol, 7-octene-1-ol, 8-nonene-1-ol, 9-decene-1-ol, 10-undecene-1-ol, more preferably one or more of 4-pentene-1-ol, 4-pentene-2-ol, 9-decene-1-ol and 10-undecene-1-ol.

[0034] According to a second aspect of the present invention, there is provided an ethylene-hydroxyl-containing α-olefin copolymer prepared by the method for preparing the ethylene-hydroxyl-containing α-olefin copolymer according to the first aspect of the present invention.

[0035] Through the above technical scheme, the present invention can provide a new method for preparing ethylene-hydroxyl-containing α-olefin copolymer and the prepared ethylene-hydroxyl-containing α-olefin copolymer. According to the method of the present invention, the catalytic activity and the comonomer insertion rate can be further improved. DETAILED DESCRIPTION

[0036] The endpoints and any values ​​of the ranges disclosed in this article are not limited to the precise ranges or values, and these ranges or values ​​should be understood to include values ​​close to these ranges or values. For numerical ranges, the endpoint values ​​of each range, the endpoint values ​​of each range and the individual point values, and the individual point values ​​can be combined with each other to obtain one or more new numerical ranges, which should be considered as specifically disclosed in this article.

[0037] The first aspect of the present invention provides a method for preparing an ethylene-hydroxyl-containing α-olefin copolymer, wherein the method comprises: using a catalyst composition to copolymerize ethylene and a hydroxyl-containing α-olefin,

[0038] Wherein, the catalyst composition comprises the following components:

[0039] a) a transition metal compound having a structure represented by formula (1);

[0040] b) a co-catalyst component,

[0041]

[0042] In formula (1), M is a tetravalent transition metal atom; X and Y are each independently a hydrocarbonoxy group having 1 to 10 carbon atoms or a halogen.

[0043] According to the present invention, in formula (1), M is a tetravalent transition metal atom, preferably, M is a titanium atom, a zirconium atom or a hafnium atom; more preferably, M is a titanium atom or a zirconium atom.

[0044] According to the present invention, in formula (1), X and Y are each independently a hydrocarbyloxy group having 1 to 10 carbon atoms or a halogen; preferably, X and Y are each independently a hydrocarbyloxy group having 1 to 6 carbon atoms, a fluorine atom, a chlorine atom, a bromine atom or an iodine atom; more preferably, X and Y are each independently a hydrocarbyloxy group having 1 to 3 carbon atoms or a chlorine atom.

[0045] Examples of the hydrocarbonoxy group having 1 to 10 carbon atoms include methoxy, ethoxy, propoxy, isopropoxy, butoxy, tert-butoxy, sec-butoxy, isobutoxy, pentyloxy, and hexyloxy. Among them, methoxy, ethoxy, propoxy, and isopropoxy are preferred, ethoxy, propoxy, and isopropoxy are more preferred, and ethoxy and isopropoxy are still more preferred.

[0046] Examples of the halogen atom include fluorine, chlorine, bromine and iodine, preferably fluorine, chlorine or bromine, more preferably chlorine or bromine, and particularly preferably chlorine.

[0047] In a particularly preferred embodiment of the present invention, X and Y are both isopropoxy or ethoxy.

[0048] In another particularly preferred embodiment of the present invention, X and Y are both chlorine atoms.

[0049] As specific transition metal compounds, preferably the following compounds can be mentioned:

[0050] In formula (1), M is a titanium atom, and X and Y are both isopropoxy groups;

[0051] In formula (1), M is a titanium atom, and X and Y are both ethoxy groups;

[0052] In formula (1), M is a titanium atom, and X and Y are both chlorine atoms;

[0053] In formula (1), M is a zirconium atom, and X and Y are both isopropoxy groups;

[0054] In formula (1), M is a zirconium atom, and X and Y are both ethoxy groups;

[0055] In formula (1), M is a zirconium atom, and X and Y are both chlorine atoms;

[0056] In formula (1), M is a hafnium atom, and X and Y are both isopropoxy groups;

[0057] In formula (1), M is a hafnium atom, and X and Y are both ethoxy groups;

[0058] In formula (1), M is a hafnium atom, and X and Y are both chlorine atoms.

[0059] According to the present invention, the co-catalyst component can be various co-catalyst components commonly used in the art. Preferably, the co-catalyst component includes a combination of alkylaluminoxane, an organoboron compound and an organoaluminum compound, or a combination of an organoaluminum compound and an organomagnesium compound; more preferably, the co-catalyst component is a combination of alkylaluminoxane, an organoboron compound and an organoaluminum compound, or a combination of an organoaluminum compound and an organomagnesium compound.

[0060] In a particularly preferred embodiment of the present invention, the co-catalyst component is a combination of an organoaluminum compound and an organomagnesium compound, thereby being able to significantly improve the catalytic activity.

[0061] The alkylaluminoxane is preferably a compound selected from the group consisting of compounds represented by formula (2) and / or formula (3).

[0062]

[0063] In formula (2) and formula (3), R is selected from an alkyl group having 1 to 15 carbon atoms, and n is an integer of 4 to 30; more preferably, R is selected from an alkyl group having 1 to 5 carbon atoms, and n is an integer of 10 to 30.

[0064] Specific examples of the above-mentioned alkyl group include methyl, ethyl, propyl, isopropyl, butyl, tert-butyl, sec-butyl, isobutyl, pentyl, 1,1-dimethylpropyl, 1,2-dimethylpropyl, neopentyl, 1-methylbutyl, 2-methylbutyl, isopentyl, hexyl, heptyl, octyl, nonyl, decyl, undecyl, dodecyl, tridecyl, tetradecyl and pentadecyl.

[0065] Examples of n include 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, and 30.

[0066] Specific examples of the alkylaluminoxane include methylaluminoxane, ethylaluminoxane, propylaluminoxane and the like, and among them, methylaluminoxane is preferred.

[0067] According to the present invention, the organic boron compound can be various organic boron compounds used as co-catalysts in the art, for example, one or more of triphenylmethyl tetrakis(pentafluorophenyl)borate, N,N-dimethylaniline tetrakis(pentafluorophenyl)borate and tris(pentafluorophenyl)boron.

[0068] According to the present invention, the organoaluminum compound can be various organoaluminum compounds used as co-catalysts in the art. Preferably, the organoaluminum compound is a compound having a structure shown in the general formula AlX1X2X3, wherein X1, X2 and X3 are respectively a halogen atom, an alkyl group having 1 to 8 carbon atoms, an alkoxy group having 1 to 8 carbon atoms, and an aryloxy group having 6 to 12 carbon atoms, and X1, X2 and X3 can be the same or different, and at least one is an alkyl group having 1 to 8 carbon atoms.

[0069] Examples of the alkyl group having 1 to 8 carbon atoms include methyl, ethyl, propyl, isopropyl, butyl, tert-butyl, sec-butyl, isobutyl, pentyl, 1,1-dimethylpropyl, 1,2-dimethylpropyl, neopentyl, 1-methylbutyl, 2-methylbutyl, isopentyl, hexyl, heptyl, and octyl.

[0070] Examples of the alkoxy group having 1 to 8 carbon atoms include various alkoxy groups having the above-mentioned "alkyl group having 1 to 8 carbon atoms" specifically exemplified.

[0071] Examples of the halogen atom include fluorine, chlorine, bromine and iodine, preferably fluorine, chlorine or bromine, more preferably chlorine or bromine, and particularly preferably chlorine.

[0072] In the present invention, specific examples of the organic aluminum compound include: one or more of trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, triisopropylaluminum, tri-sec-butylaluminum, tricyclopentylaluminum, tri-n-pentylaluminum, triisopentylaluminum, trihexylaluminum, ethyldimethylaluminum, methyldiethylaluminum, tripentylaluminum, diethylaluminum chloride and dimethylaluminum chloride.

[0073] In the present invention, when the co-catalyst component is a combination of an organic boron compound and an organic aluminum compound, specific examples of the organic aluminum compound include: one or more of trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, triisopropylaluminum, tri-sec-butylaluminum, tricyclopentylaluminum, tri-n-pentylaluminum, triisopentylaluminum, trihexylaluminum, ethyldimethylaluminum, methyldiethylaluminum and tripentylaluminum. Among them, triisobutylaluminum is preferably used.

[0074] In the present invention, when the co-catalyst component is a combination of an organoaluminum compound and an organomagnesium compound, the organoaluminum compound preferably contains at least one hydrocarbon group and at least one halogen atom, more preferably dialkylaluminum chloride, further preferably diethylaluminum chloride or dimethylaluminum chloride.

[0075] In the present invention, the organic magnesium compound is preferably an organic magnesium compound containing two alkyl groups with carbon atoms of 1 to 10, and more preferably an organic magnesium compound containing two alkyl groups with carbon atoms of 1 to 6. For example, dimethyl magnesium, diethyl magnesium, di-n-propyl magnesium, di-n-butyl magnesium, di-n-pentyl magnesium, di-n-hexyl magnesium, etc. are mentioned, among which di-n-propyl magnesium, di-n-butyl magnesium and di-n-pentyl magnesium are preferably one or more, and di-n-butyl magnesium is more preferably.

[0076] According to the present invention, when the co-catalyst component is alkylaluminoxane, the molar ratio of the transition metal compound to the alkylaluminoxane calculated as aluminum is 1:(100-20000), preferably 1:(200-10000), and more preferably 1:(500-5000).

[0077] When the co-catalyst component is a combination of an organic boron compound and an organic aluminum compound, the molar ratio of the transition metal compound to the organic boron compound is 1:(1-5), preferably 1:(1-2), and the molar ratio of the transition metal compound to the organic aluminum compound is 1:(10-5000), preferably 1:(50-1000), and more preferably 1:(100-500).

[0078] When the co-catalyst component is a combination of an organoaluminum compound and an organomagnesium compound, the molar ratio of the transition metal compound to the organoaluminum compound is 1:(30-5000), preferably 1:(100-1000), more preferably 1:(100-500), and the molar ratio of the transition metal compound to the organomagnesium compound is 1:(10-2000), preferably 1:(100-1000). In addition, the molar ratio of the organoaluminum compound to the organomagnesium compound is preferably greater than 2.5:1.

[0079] According to the present invention, preferably, the hydroxyl-containing α-olefin is reacted with an alkyl aluminum before use, and the alkyl aluminum is an aluminum compound containing three alkyl groups with carbon atoms of 2-8, preferably triethyl aluminum and / or triisobutyl aluminum.

[0080] In addition, the molar ratio of the alkyl aluminum to the hydroxyl-containing α-olefin may be 1.0-2.0:1, preferably 1.0-1.2:1.

[0081] In the present invention, "the hydroxy-containing α-olefin is reacted with the alkyl aluminum before use" includes: the case where the hydroxy-containing α-olefin and the alkyl aluminum are mixed and reacted in advance and then added to the reaction system as a mixed component, and also includes: the case where the hydroxy-containing α-olefin and the alkyl aluminum are added to the reaction system at the same time.

[0082] In addition, it should be noted that the alkylaluminum used here is not included in the amount of the above-mentioned organoaluminum compound.

[0083] According to the present invention, preferably, the concentration of the transition metal compound in the copolymerization reaction system is 1×10 -10 mol / L~1×10 -3 mol / L, preferably 1×10 -8 mol / L~1×10 -5 mol / L.

[0084] According to the present invention, the amounts of ethylene and the hydroxyl-containing α-olefin used can be the amounts commonly used in the art for synthesizing ethylene-hydroxyl-containing α-olefin copolymers. For example, the concentration of the hydroxyl-containing α-olefin in the polymerization reaction system is 0.001-1 mol / L, preferably 0.01-0.5 mol / L.

[0085] In addition, the amount of olefin used may be 1,000-1,000,000 molar equivalents of the catalyst.

[0086] According to the present invention, preferably, the copolymerization reaction is carried out in an inert organic solvent. The inert organic solvent may be a mixture of one or more of a straight-chain aliphatic hydrocarbon, a branched aliphatic hydrocarbon, a substituted or unsubstituted cyclic aliphatic hydrocarbon, and a substituted or unsubstituted aromatic hydrocarbon. Specific examples of the inert organic solvent include: hexane, heptane, cyclohexane, cyclooctane, toluene, and xylene. In addition, the amount of the organic solvent may be determined according to the reaction activity to ensure that the produced polymer is well dissolved in the system, at least without affecting the dispersion.

[0087] According to the method of the present invention, the copolymerization reaction conditions can be the common conditions used in the art for synthesizing ethylene-hydroxyl-containing α-olefin copolymers. Preferably, the copolymerization reaction temperature is -50 to 200°C, and the copolymerization reaction time is 1 to 300 minutes; more preferably, the copolymerization reaction temperature is -20 to 150°C, and the copolymerization reaction time is 5 to 60 minutes.

[0088] According to the method of the present invention, preferably, the partial pressure of ethylene is 0.1-10 MPa, preferably 0.1-4.0 MPa.

[0089] According to the present invention, preferably, the hydroxyl-containing α-olefin is a terminal olefin containing 3 to 18 carbon atoms and containing more than one hydroxyl group, preferably allyl alcohol, 3-butene-1-ol, 4-pentene-1-ol, 4-pentene-2-ol, 5-hexene-1-ol, 6-heptene-1-ol, 7-octen-1-ol, 8-nonene-1-ol, 9-decene-1-ol, 10-undecene-1-ol, more preferably one or more of 4-pentene-1-ol, 4-pentene-2-ol, 9-decene-1-ol and 10-undecene-1-ol.

[0090] In the present invention, the transition metal compound can be synthesized according to conventional methods in the art. In a preferred embodiment of the present invention, when X and Y in formula (1) are each independently a hydrocarbon oxy group having 1 to 10 carbon atoms, the preparation method of the transition metal compound comprises: in an inert atmosphere and in the presence of a first organic solvent, a first contact reaction is carried out between 10-hydroxybenzo[H]quinoline and a compound represented by the general formula MA4 (hereinafter referred to as method 1).

[0091] In method 1, in the compound represented by the general formula MA4, M is a tetravalent transition metal atom; and A is independently a hydrocarbonoxy group having 1 to 10 carbon atoms.

[0092] Preferably, M is a titanium atom, a zirconium atom or a hafnium atom, more preferably a titanium atom or a zirconium atom.

[0093] Preferably, each A is independently a hydrocarbyloxy group having 1 to 6 carbon atoms; more preferably, each A is independently a hydrocarbyloxy group having 1 to 3 carbon atoms.

[0094] Examples of the hydrocarbonoxy group having 1 to 10 carbon atoms include methoxy, ethoxy, propoxy, isopropoxy, butoxy, tert-butoxy, sec-butoxy, isobutoxy, pentyloxy, and hexyloxy. Among them, methoxy, ethoxy, propoxy, and isopropoxy are preferred, ethoxy, propoxy, and isopropoxy are more preferred, and ethoxy and isopropoxy are still more preferred.

[0095] In method 1, the molar ratio of 10-hydroxybenzo[H]quinoline to the compound represented by the general formula MA4 can be 1.8-2.2:1, preferably 1.9-2.1:1, and more preferably 1.95-2.05:1.

[0096] In method 1, the first organic solvent may be an organic solvent that is inert to the reaction raw materials and can dissolve the reaction raw materials, for example, toluene may be used. The amount of the organic solvent may be selected according to the amount of 10-hydroxybenzo[H]quinoline, for example, the amount of the first organic solvent relative to 1 mol of 10-hydroxybenzo[H]quinoline is 5-30 L, preferably 6-20 L, more preferably 7-15 L, and particularly preferably 8-10 L.

[0097] In method 1, the inert atmosphere may be implemented by using nitrogen gas and / or argon gas.

[0098] In method 1, the conditions of the first contact reaction can be selected according to the boiling point of the first organic solution used, for example, the reaction can be carried out under reflux conditions for 5-20 hours, preferably 5-10 hours.

[0099] In method 1, after the first contact reaction is completed, the product may be purified by a conventional purification method in the art. For example, after the first contact reaction is completed, the solvent may be removed and washing may be performed to obtain the target product.

[0100] In a preferred embodiment of the present invention, after the first contact reaction is completed, the solvent is removed, and then centrifugal washing is performed 2-3 times using ice-cold hexane to obtain the target product.

[0101] In addition, when X and Y in formula (1) are each independently a halogen, the preparation method of the transition metal compound comprises: in an inert atmosphere and in the presence of a second organic solvent, subjecting 10-hydroxybenzo[H]quinoline to a second contact reaction with an n-butyllithium solution, and then subjecting it to a third contact reaction with a compound represented by MX4 (hereinafter referred to as method 2).

[0102] In method 2, in the compound represented by the general formula MX4, M is a tetravalent transition metal atom; and X is independently a halogen.

[0103] Preferably, M is a titanium atom, a zirconium atom or a hafnium atom, more preferably a titanium atom or a zirconium atom.

[0104] Examples of the halogen atom include fluorine, chlorine, bromine and iodine, preferably fluorine, chlorine or bromine, more preferably chlorine or bromine, and particularly preferably chlorine.

[0105] In method 2, the molar ratio of 10-hydroxybenzo[H]quinoline to n-butyllithium can be 1:0.95-1.5, preferably 1:1-1.2, and more preferably 1:1-1.1.

[0106] As the above-mentioned n-butyl lithium solution, for example, n-butyl lithium hexane solution can be used. When used in the form of a solution, the content of n-butyl lithium in the solution can be, for example, 1-3 mol / L, preferably 2-3 mol / L, and more preferably 2-2.5 mol / L.

[0107] In method 2, the second organic solvent may be an organic solvent that is inert to the reaction raw materials and can dissolve the reaction raw materials, for example, toluene may be used. The amount of the organic solvent may be selected according to the amount of 10-hydroxybenzo[H]quinoline, for example, relative to 1 mol of 10-hydroxybenzo[H]quinoline, the amount of the first organic solvent is 5-30 L, preferably 6-20 L, more preferably 7-15 L, and particularly preferably 7-9 L.

[0108] In method 2, the inert atmosphere may be implemented by using nitrogen and / or argon.

[0109] In method 2, the second contact reaction is preferably carried out by dropwise adding an n-butyl lithium solution into a mixed solution of 10-hydroxybenzo[H]quinoline and the second organic solvent.

[0110] The temperature of the second contact reaction during the dropwise addition may be -30 to 0° C., preferably -20 to -10° C. After the dropwise addition is completed, the reaction may be carried out at room temperature (eg, 10 to 40° C.) for 5 to 36 hours, preferably 12 to 24 hours.

[0111] In method 2, the molar ratio of 10-hydroxybenzo[H]quinoline to the compound represented by the general formula MX4 can be 1.8-2.2:1, preferably 1.9-2.1:1, and more preferably 1.95-2.05:1.

[0112] In method 2, the third contact reaction is preferably carried out by dropwise adding the n-butyllithium solution into the product of the first contact reaction to carry out the third contact reaction.

[0113] The temperature of the third contact reaction during the dropwise addition may be -30 to 0° C., preferably -20 to -10° C. After the dropwise addition is completed, the reaction may be carried out at room temperature (eg, 10 to 40° C.) for 5 to 36 hours, preferably 12 to 24 hours.

[0114] In method 2, after the third contact reaction is completed, the product may be purified by a conventional purification method in the art. For example, after the third contact reaction is completed, the solvent may be removed and washing may be performed to obtain the target product.

[0115] In a preferred embodiment of the present invention, after the third contact reaction is completed, a solid phase is obtained by solid-liquid separation, and centrifugation washing is performed 2-3 times using ice-cold hexane to obtain the target product.

[0116] In addition, in the present invention, the target product in method 2 can be prepared by replacing the hydrocarbon group with 1-10 carbon atoms in the target product obtained by method 1 with a halogen group; similarly, the target product in method 2 can be prepared by replacing the halogen group with a hydrocarbon group with 1-10 carbon atoms. The specific method can be implemented by conventional synthesis methods in the art.

[0117] According to a second aspect of the present invention, there is provided an ethylene-hydroxyl-containing α-olefin copolymer prepared by the method for preparing the ethylene-hydroxyl-containing α-olefin copolymer according to the first aspect of the present invention.

[0118] The present invention will be described in detail below by way of examples, but the present invention is not limited to the following examples.

[0119] The raw materials used in the following examples and comparative examples, unless otherwise specified, are all disclosed in the prior art, for example, they can be directly purchased or prepared according to the preparation method disclosed in the prior art.

[0120] In the following examples and comparative examples, the comonomer content was tested using the following method.

[0121] The comonomer content of the sample was tested using an AVANCE III 400MHz nuclear magnetic resonance spectrometer produced by Bruker. The solvent was deuterated o-dichlorobenzene, and a 10 mm PASEX 13C-1H / D Z-GRD probe was used to dissolve a sample with a mass concentration of 10% at 130°C. The test temperature was 125°C, the rotation speed was 20 Hz, the pulse was 90°, the spectrum width was 120 ppm, the sampling time was 5 seconds, the delay time was 10 seconds, and the scan was 6000 times. 13 The comonomer content was calculated from the C-NMR spectrum using the method described in the literature (e.g. Macromolecular Chemistry and Physics, 2013, 214, 2245-2249).

[0122] Preparation Example 1

[0123] Synthesis of compound (1):

[0124]

[0125] Place the magnet in a dry 250 ml three-necked flask, and place the reaction flask on a device with magnetic stirring and oil bath heating. After evacuating the three-necked flask, rinse it repeatedly with nitrogen three times, add 470 mg of 10-hydroxybenzo[H]quinoline under nitrogen atmosphere, add 20 ml of toluene and stir at room temperature to dissolve; add 10 ml of toluene solution of tetra(isopropoxy)titanium (containing 342 mg of tetra(isopropoxy)titanium) and stir evenly. Then, under nitrogen protection, add a condenser with room temperature water as the cooling medium. Control the oil bath temperature at 115-130°C and allow the reaction to proceed for 8 hours under toluene reflux. Then remove the reflux condenser, install a distillation device, maintain the temperature, and evaporate the liquid of the reaction mixture until a yellow solid or viscous substance is obtained, and then cool it to room temperature. Under nitrogen protection, add 10 ml of cold hexane, mix thoroughly, and centrifuge the resulting slurry. Pour out the supernatant. Add 10 ml of cold hexane again, mix thoroughly, and centrifuge the resulting slurry. The supernatant was poured off, and the solvent of the obtained solid was removed under vacuum to obtain 641 mg of bright yellow solid with a molar yield of 96%.

[0126] 1 H-NMR(in CDCl3,d=):9.09-9.11(2H),7.71-7.73(2H),7.52-7.56(2H),7.46-7.49 (2H),7.14-7.19(6H),6.89-6.92(2H),4.84-4.91(2H),1.07-1.19(12H).

[0127] 13 C-NMR (in CDCl3, d=): 161.3, 148.9, 143.7, 135.9, 134.5, 128.8, 127.9, 125.3, 123.3, 118.8, 118.5, 116.5, 115.4, 77.0, 24.3.

[0128] Preparation Example 2

[0129] Synthesis of compound (2):

[0130]

[0131] Place the magnet in a dry 250 ml three-necked flask, evacuate the flask and rinse it with nitrogen three times, add 500 mg of 10-hydroxybenzo[H]quinoline under nitrogen atmosphere, add 20 ml of toluene and stir at room temperature to dissolve, place the three-necked flask in a low-temperature magnetic stirring device, and stir at -20°C for 20 minutes. Take 1.1 ml of n-butyl lithium solution (2.5 mol / L hexane solution) and slowly add it dropwise. After the addition is complete, naturally warm to room temperature and stir to react overnight. Place the three-necked flask in a low-temperature magnetic stirring device and stir at -20°C for 20 minutes. Dissolve 243 mg of titanium tetrachloride in 10 ml of toluene at -20°C and slowly add it dropwise to the three-necked flask. After the addition is complete, naturally warm to room temperature and stir to react overnight. The obtained reaction slurry was filtered through diatomaceous earth, and the filter cake was washed with toluene. The obtained dark red solution was desolventized under vacuum to obtain a dark red solid. 10 ml of cold hexane was added, and after thorough mixing, the obtained slurry was centrifuged and the supernatant was poured out. 10 ml of cold hexane was added again, and after thorough mixing, the obtained slurry was centrifuged and the supernatant was poured out. The obtained solid was desolventized under vacuum to obtain 590 mg of a dark red solid with a molar yield of 91%.

[0132] The structure of the dark red solid was confirmed to be compound (2) by H-NMR and C-NMR.

[0133] Preparation Example 3

[0134] Synthesis of compound (3):

[0135]

[0136] Place the magnet in a dry 250 ml three-necked flask, evacuate the flask and rinse it with nitrogen three times, add 586 mg of 10-hydroxybenzo[H]quinoline under nitrogen atmosphere, add 20 ml of toluene and stir at room temperature to dissolve, place the three-necked flask in a low-temperature magnetic stirring device, and stir at -20°C for 20 minutes. Take 1.3 ml of n-butyl lithium solution (2.5 mol / L hexane solution) and slowly add it dropwise. After the addition is complete, warm to room temperature naturally and stir to react overnight. Place the three-necked flask in a low-temperature magnetic stirring device and stir at -20°C for 20 minutes. Under nitrogen protection, add 350 mg of zirconium tetrachloride solid to the three-necked flask three times, with an interval of 2 minutes each time. After completion, warm to room temperature naturally and stir to react overnight. The obtained reaction slurry was filtered through diatomaceous earth, and the filter cake was washed with toluene. The obtained red solution was freed of solvent under vacuum to obtain a red solid. 10 ml of cold hexane was added and mixed thoroughly. The obtained slurry was centrifuged and the supernatant was poured out. 10 ml of cold hexane was added again and mixed thoroughly. The obtained slurry was centrifuged and the supernatant was poured out. The obtained solid was freed of solvent under vacuum to obtain 675 mg of dark red solid with a molar yield of 82%.

[0137] The structure of the dark red solid was confirmed to be compound (3) by H-NMR and C-NMR.

[0138] Preparation Example 4

[0139] Synthesis of compound (4):

[0140]

[0141] Place the magnet in a dry 250 ml three-necked flask, and place the reaction flask on a device for magnetic stirring and oil bath heating. After evacuating the three-necked flask, rinse it repeatedly with nitrogen three times. Add 426 mg of 10-hydroxybenzo[H]quinoline, 296 mg of tetra(ethoxy)zirconium, and 20 ml of toluene under a nitrogen atmosphere, and stir evenly at room temperature. Then, under nitrogen protection, add a condenser with room temperature water as the cooling medium. Control the oil bath temperature at 115-130°C and allow the reaction to proceed under toluene reflux for 18 hours. Cool to room temperature, filter the solution, and remove the solvent in vacuum to obtain a light yellow solid or viscous material. Under nitrogen protection, add 10 ml of cold hexane, mix thoroughly, centrifuge the resulting slurry, pour out the supernatant, and remove the solvent from the resulting solid under vacuum to obtain 482 mg of a light yellow solid with a molar yield of 78%.

[0142] The structure of the light yellow solid was confirmed to be compound (4) by hydrogen and carbon nuclear magnetic spectra.

[0143] Preparation Example 5

[0144] Synthesis of compound (5):

[0145]

[0146] Place the magnet in a dry 250 ml three-necked flask, evacuate the flask and rinse it with nitrogen three times, add 575 mg of 10-hydroxybenzo[H]quinoline under nitrogen atmosphere, add 20 ml of toluene and stir at room temperature to dissolve, place the three-necked flask in a low-temperature magnetic stirring device, and stir at -20°C for 20 minutes. Take 1.3 ml of n-butyl lithium solution (2.5 mol / L hexane solution) and slowly add it dropwise. After the addition is complete, naturally warm to room temperature and stir to react overnight. Place the three-necked flask in a low-temperature magnetic stirring device and stir at -20°C for 20 minutes. Under nitrogen protection, add 470 mg of zirconium tetrachloride solid to the three-necked flask three times, with an interval of 2 minutes each time. After completion, naturally warm to room temperature and stir to react overnight. The obtained reaction slurry was filtered through diatomaceous earth, and the filter cake was washed with toluene. The obtained red solution was desolventized under vacuum to obtain a red solid. 10 ml of cold hexane was added and mixed thoroughly. The obtained slurry was centrifuged and the supernatant was poured out. 10 ml of cold hexane was added again and mixed thoroughly. The obtained slurry was centrifuged and the supernatant was poured out. The obtained solid was desolventized under vacuum to obtain 712 mg of dark red solid with a molar yield of 76%.

[0147] The structure of the dark red solid was confirmed to be compound (5) by H-NMR and C-NMR.

[0148] Example 1

[0149] Copolymerization of ethylene-4-pentene-1-ol using compound (1) as catalyst

[0150] A 250 ml glass polymerization bottle was dried thoroughly, evacuated, and flushed with nitrogen, and repeated three times. Evacuate the bottle and fill it with ethylene, the ethylene pressure is 1.05 standard atmospheres, and add 23 ml of toluene, 0.2 ml of 4-penten-1-ol, 2 ml of triisobutylaluminum toluene solution (containing 2.0 mmol of triisobutylaluminum), and 3 ml of methylaluminoxane toluene solution (containing 5.0 mmol of methylaluminoxane) in sequence, start stirring and heating, and set the temperature to 70°C. When the temperature rises to 70°C, add 1 ml of catalyst toluene solution (containing 5 micromoles of compound (1)), start timing, and replenish ethylene when ethylene is consumed so that the ethylene pressure is always kept at a constant 1.05 standard atmospheres. After 20 minutes, turn off ethylene, pour the reaction solution into a beaker, add 300 ml of anhydrous ethanol and 5 ml of concentrated hydrochloric acid, stir for 6 hours, filter to obtain a polymer, and vacuum dry at 60°C for 24 hours to obtain 0.32 g of polymer. The polymerization activity is 192 kg polymer / mol catalyst / hour, and the results are shown by nuclear magnetic resonance. 13 The 4-penten-1-ol content was determined by C-NMR and was 3.3 mol%.

[0151] Example 2

[0152] Copolymerization of ethylene-4-pentene-1-ol using compound (1) as catalyst

[0153] A 250 ml glass polymerizer bottle that has been fully dried is evacuated and flushed with nitrogen, and this process is repeated three times. The bottle is evacuated and filled with ethylene under the control of a solenoid valve, and the ethylene pressure is 1.05 standard atmospheric pressure. 24 ml of toluene, 0.2 ml of 4-pentene-1-ol, and 3 ml of triisobutylaluminum toluene solution (containing 3.0 mmol of triisobutylaluminum) are added in sequence, and stirring and heating are started, with the temperature set at 70°C. When the temperature reaches 70°C, 1 ml of a catalyst toluene solution (containing 5 micromoles of compound (1)) is added. After 3 minutes, 1 ml of a triphenylmethyl tetrakis(pentafluorophenyl)borate toluene solution (containing 7.5 micromoles of triphenylmethyl tetrakis(pentafluorophenyl)borate) is added, and timing is started. When ethylene is consumed, ethylene is replenished to keep the ethylene pressure at a constant 1.05 standard atmospheric pressure. After 20 minutes, ethylene was turned off, the reaction solution was poured into a beaker, 300 ml of anhydrous ethanol and 5 ml of concentrated hydrochloric acid were added, and the mixture was stirred for 6 hours. The polymer was filtered and dried under vacuum at 60°C for 24 hours to obtain 0.28 g of polymer. The polymerization activity was 168 kg polymer / mol catalyst / hour, and the results were obtained by nuclear magnetic resonance. 13 The 4-penten-1-ol content was determined by C-NMR and was 3.7 mol%.

[0154] Example 3

[0155] Copolymerization of ethylene-4-pentene-1-ol using compound (1) as catalyst

[0156] A 250 ml glass polymer bottle that has been fully dried is evacuated and flushed with nitrogen, and this process is repeated three times. The bottle is evacuated and filled with ethylene under the control of a solenoid valve, and the ethylene pressure is 1.05 standard atmospheric pressure. 23 ml of toluene, 0.2 ml of 4-penten-1-ol, and 2.0 ml of triethylaluminum toluene solution (containing 2.0 mmol of triethylaluminum) are added in sequence. Three minutes later, 2.5 ml of diethylaluminum chloride toluene solution (containing 2.5 mmol of diethylaluminum chloride) is added, and magnetic stirring and heating are started, with the temperature set at 70°C. When the temperature reaches 70°C, 1 ml of a catalyst toluene solution (containing 5 micromoles of compound (1)) is added. Three minutes later, 0.5 ml of di-n-butylmagnesium toluene solution (containing 0.5 mmol of di-n-butylmagnesium) is added, and timing is started. When ethylene is consumed, the solenoid valve automatically opens to replenish ethylene, so that the ethylene pressure is always kept constant at 1.05 standard atmospheric pressure. After 20 minutes, ethylene was turned off, the reaction solution was poured into a beaker, 300 ml of anhydrous ethanol and 5 ml of concentrated hydrochloric acid were added, and the mixture was stirred for 6 hours. The polymer was filtered and dried under vacuum at 60°C for 24 hours to obtain 0.47 g of polymer. The polymerization activity was 282 kg polymer / mol catalyst / hour, and the results were obtained by nuclear magnetic resonance. 13 The 4-penten-1-ol content was determined by C-NMR and was 2.4 mol%.

[0157] Example 4

[0158] Copolymerization of ethylene-4-pentene-1-ol using compound (1) as catalyst

[0159] A 100 ml stainless steel polymerization kettle was fully dried, and the empty kettle was heated to 55°C and evacuated for 30 minutes. Ethylene was charged to maintain a weak ethylene flow. 30 ml toluene, 1 ml 4-penten-1-ol, 10 ml triethylaluminum toluene solution (containing 10 mmol of triethylaluminum) were added. Five minutes later, 2.5 ml diethylaluminum chloride toluene solution (containing 2.5 mmol of diethylaluminum chloride) were added, stirring was started, the temperature was adjusted to 60°C, 1 ml catalyst toluene solution (containing 2 micromoles of compound (1)) was added, 60°C was stabilized after 3 minutes, 0.5 ml di-n-butylmagnesium toluene solution (containing 0.5 mmol of di-n-butylmagnesium) was added, and the feed port was closed. The ethylene pressure was adjusted to 6 standard atmospheres. After 30 minutes, the ethylene was turned off, the temperature was lowered, and the pressure was slowly released. The polymerization reaction mixture was poured into 500 ml of anhydrous ethanol containing 10 ml of concentrated hydrochloric acid, and the polymer was filtered to obtain a polymer, which was vacuum dried at 60°C for 24 hours to obtain 4.28 g of a polymer. Polymerization activity 4280 kg polymer / mol catalyst / hour, by NMR 13 The 4-penten-1-ol content was determined by C-NMR and was 5.9 mol%.

[0160] Example 5

[0161] Copolymerization of ethylene-4-pentene-1-ol using compound (2) as catalyst

[0162] The method of Example 1 was followed, except that compound (1) was replaced by the same molar amount of compound (2), and 0.35 g of polymer was obtained in the same manner. The polymerization activity was 210 kg polymer / mol catalyst / hour, and the results of nuclear magnetic resonance spectroscopy showed that the polymerization activity was 210 kg polymer / mol catalyst / hour, and ... 13 The 4-penten-1-ol content was determined by C-NMR and was 3.5 mol%.

[0163] Example 6

[0164] Ethylene-4-pentene-1-ol copolymerization catalyzed by compound (3)

[0165] The method of Example 1 was followed, except that compound (1) was replaced by the same molar amount of compound (3), and 0.41 g of polymer was obtained in the same manner. The polymerization activity was 246 kg polymer / mol catalyst / hour, and the results of nuclear magnetic resonance spectroscopy showed that the polymerization activity was 246 kg polymer / mol catalyst / hour, and ... 13 The 4-penten-1-ol content was determined by C-NMR and was 3.9 mol%.

[0166] Example 7

[0167] Copolymerization of ethylene and 4-pentene-1-ol using compound (4) as catalyst

[0168] The method of Example 1 was followed, except that compound (1) was replaced by the same molar amount of compound (4), and 0.39 g of polymer was obtained in the same manner. The polymerization activity was 234 kg polymer / mol catalyst / hour, and the results of nuclear magnetic resonance spectroscopy showed that the polymerization activity was 234 kg polymer / mol catalyst / hour, and ... 13 The 4-penten-1-ol content was determined by C-NMR and was 3.6 mol%.

[0169] Example 8

[0170] Copolymerization of ethylene-4-pentene-1-ol using compound (5) as catalyst

[0171] The method of Example 1 was followed, except that compound (1) was replaced by the same molar amount of compound (5), and 0.40 g of polymer was obtained in the same manner. The polymerization activity was 240 kg polymer / mol catalyst / hour, and the results of nuclear magnetic resonance spectroscopy showed that the polymerization activity was 240 kg polymer / mol catalyst / hour, and ... 13 The 4-penten-1-ol content was determined by C-NMR and was 4.1 mol%.

[0172] Comparative Example 1

[0173] Copolymerization of Ethylene-4-Pentene-1-ol Catalyzed by Zirconocene Dichloride

[0174] The method of Example 1 was followed, except that the compound (1) was replaced by the same molar amount of zirconocene dichloride, and 0.02 g of polymer was obtained in the same manner. The polymerization activity was 12 kg polymer / mol catalyst / hour.

[0175] Comparative Example 2

[0176] Copolymerization of Ethylene-4-Pentene-1-ol Catalyzed by Zirconocene Dichloride

[0177] The method of Example 2 was followed, except that compound (1) was replaced with the same molar amount of zirconocene dichloride, and 0.15 g of polymer was obtained. The polymerization activity was 90 kg polymer / mol catalyst / hour, and the results were analyzed by nuclear magnetic resonance. 13 The 4-penten-1-ol content was determined by C-NMR and was 2.2 mol%.

[0178] Comparative Example 3

[0179] Copolymerization of Ethylene-4-Pentene-1-ol Catalyzed by Zirconocene Dichloride

[0180] The method of Example 3 was followed, except that compound (1) was replaced by the same molar amount of zirconocene dichloride, and 0.2 g of polymer was obtained. The polymerization activity was 120 kg polymer / mol catalyst / hour, and the results were analyzed by nuclear magnetic resonance.13 The 4-penten-1-ol content was determined by C-NMR and was 2.3 mol%.

[0181] The preferred embodiments of the present invention are described in detail above, but the present invention is not limited thereto. Within the technical concept of the present invention, the technical solution of the present invention can be subjected to a variety of simple modifications, including the combination of various technical features in any other suitable manner, and these simple modifications and combinations should also be regarded as the contents disclosed by the present invention and belong to the protection scope of the present invention.

Claims

1. A method for preparing an ethylene-hydroxyl-containing α-olefin copolymer, characterized in that: The method comprises: using a catalyst composition to copolymerize ethylene and a hydroxyl-containing α-olefin, Wherein, the catalyst composition comprises the following components: a) a transition metal compound having a structure represented by formula (1); b) a co-catalyst component, In formula (1), M is a tetravalent transition metal atom; X and Y are each independently a hydrocarbonoxy group having 1 to 10 carbon atoms or a halogen.

2. The method according to claim 1, wherein: M is a titanium atom, a zirconium atom or a hafnium atom, and is preferably a titanium atom or a zirconium atom.

3. The method according to claim 1, wherein: X and Y are each independently a hydrocarbonoxy group having 1 to 6 carbon atoms, a fluorine atom, a chlorine atom, a bromine atom or an iodine atom; Preferably, X and Y are each independently a hydrocarbonoxy group having 1 to 3 carbon atoms or a chlorine atom; Preferably, the alkoxy group having 1 to 10 carbon atoms is methoxy, ethoxy, propoxy or isopropoxy.

4. The method according to any one of claims 1 to 3, wherein: X and Y are both isopropoxy or ethoxy; or, X and Y are both chlorine atoms.

5. The method according to any one of claims 1 to 3, wherein: The co-catalyst component includes an alkylaluminoxane, a combination of an organic boron compound and an organic aluminum compound, or a combination of an organic aluminum compound and an organic magnesium compound; Preferably, the co-catalyst component is an alkylaluminoxane, a combination of an organic boron compound and an organic aluminum compound, or a combination of an organic aluminum compound and an organic magnesium compound.

6. The method according to claim 5, wherein: The alkylaluminoxane is a compound selected from the group consisting of compounds represented by formula (2) and / or formula (3), In formula (2) and formula (3), R is selected from an alkyl group having 1 to 15 carbon atoms, and n represents an integer of 4 to 30; Preferably, R is selected from an alkyl group having 1 to 5 carbon atoms, and n represents an integer of 10 to 30; Preferably, the alkylaluminoxane is methylaluminoxane.

7. The method according to claim 5, wherein: The organic boron compound is one or more of triphenylmethyl tetrakis(pentafluorophenyl)borate, N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate and tris(pentafluorophenyl)boron.

8. The method according to claim 5, wherein: The organoaluminum compound is a compound having a structure represented by the general formula AlX1X2X3, wherein X1, X2 and X3 are respectively a halogen atom, an alkyl group having 1 to 8 carbon atoms, an alkoxy group having 1 to 8 carbon atoms, and an aryloxy group having 6 to 12 carbon atoms, and X1, X2 and X3 may be the same or different, and at least one of them is an alkyl group having 1 to 8 carbon atoms; Preferably, the organoaluminum compound is triisobutylaluminum.

9. The method according to claim 5, wherein: The organomagnesium compound is an organomagnesium compound containing two alkyl groups with carbon atoms of 1 to 10, preferably an organomagnesium compound containing two alkyl groups with carbon atoms of 1 to 6, and more preferably di-n-butylmagnesium.

10. The method according to claim 5, wherein: The co-catalyst component is alkylaluminoxane, and the molar ratio of the transition metal compound to the alkylaluminoxane calculated on the basis of aluminum is 1:(100-20000), preferably 1:(200-10000), and more preferably 1:(500-5000).

11. The method according to claim 5, wherein: The co-catalyst component is a combination of an organic boron compound and an organic aluminum compound, the molar ratio of the transition metal compound to the organic boron compound is 1:(1-5), preferably 1:(1-2), the molar ratio of the transition metal compound to the organic aluminum compound is 1:(10-5000), preferably 1:(50-1000), more preferably 1:(100-500).

12. The method according to claim 5, wherein: The co-catalyst component is a combination of an organoaluminum compound and an organomagnesium compound, the molar ratio of the transition metal compound to the organoaluminum compound is 1:(30-5000), preferably 1:(100-1000), more preferably 1:(100-500), and the molar ratio of the transition metal compound to the organomagnesium compound is 1:(10-2000), preferably 1:(100-1000); Preferably, the molar ratio of the organoaluminum compound to the organomagnesium compound is greater than 2.5:

1.

13. The method according to any one of claims 1 to 3, wherein: The hydroxyl-containing α-olefin is reacted with an alkyl aluminum before use, wherein the alkyl aluminum is an aluminum compound containing three alkyl groups with a carbon number of 2 to 8, preferably triethyl aluminum and triisobutyl aluminum; Preferably, the molar ratio of the alkyl aluminum to the hydroxyl-containing α-olefin is 1.0-2.0:1, preferably 1.0-1.2:

1.

14. The method according to any one of claims 1 to 3, wherein: The concentration of the transition metal compound in the copolymerization reaction system is 1×10 -10 mol / L~1×10 -3 mol / L, preferably 1×10 -8 mol / L~1×10 -5 mol / L.

15. The method according to any one of claims 1 to 3, wherein: The copolymerization reaction temperature is -50 to 200°C, and the copolymerization reaction time is 1 to 300 minutes; Preferably, the copolymerization reaction temperature is -20 to 150° C., and the copolymerization reaction time is 5 to 60 minutes.

16. The method according to any one of claims 1 to 3, wherein: The hydroxyl-containing α-olefin is a terminal olefin containing 3 to 18 carbon atoms and one or more hydroxyl groups, preferably allyl alcohol, 3-butene-1-ol, 4-pentene-1-ol, 4-pentene-2-ol, 5-hexene-1-ol, 6-heptene-1-ol, 7-octen-1-ol, 8-nonene-1-ol, 9-decene-1-ol, 10-undecene-1-ol, more preferably one or more of 4-pentene-1-ol, 4-pentene-2-ol, 9-decene-1-ol and 10-undecene-1-ol.

17. The ethylene-hydroxyl-containing α-olefin copolymer prepared by the method for preparing the ethylene-hydroxyl-containing α-olefin copolymer according to any one of claims 1 to 16.

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