KR20110133156A - ADVANCED TRANSITION METAL CATALYTIC SYSTEMS IN TERMS OF COMONOMER INCORPORATIONS AND METHODS FOR PREPARING ETHYLENE HOMOPOLYMERS OR COPOLYMERS OF ETHYLENE AND α-OLEFINS USING THE SAME - Google Patents

Abstract

PURPOSE: A four family transition metal compound for preparing ethylene homopolymer or alpha-olefin copolymer is provided to ensure thermal stability. CONSTITUTION: A transition metal compound is denoted by chemical formula 1. A transition metal catalyst composition for preparing ethylene homopolymer or alpha-olefin copolymer contains the transition metal compound and cocatalyst of aluminum compounds, boron compounds, or mixture thereof. A comonomer polymerized with ethylene is propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 1-undecene, 1-dodecene, or 1-itocene.

Description

Advanced transition metal catalytic systems in terms of comonomer incorporations and methods for preparing ethylene homopolymers or copolymers of ethylene and α-olefins using the same}

The present invention relates to a homogeneous catalyst system for preparing copolymers of ethylene homopolymers or α-olefins, and more particularly, cyclopenta in which an alkyl group is substituted at the 3,4-position around the Group 4 transition metal, as shown in Formula 1 below. It relates to a Group 4 transition metal catalyst characterized in that a dienyl derivative and an electron donating substituent are crosslinked. The present invention also relates to a catalyst system comprising one or a mixture selected from such a transition metal catalyst and an aluminoxane promoter or a boron compound promoter, and a method for producing an ethylene homopolymer or a copolymer of ethylene and an -olefin using the same.

In the conventional production of copolymers of ethylene homopolymers or α-olefins, so-called Ziegler-Natta catalyst systems composed of a main catalyst component of a titanium or vanadium compound and a promoter component of an alkylaluminum compound have been generally used. However, the Ziegler-Natta catalyst system exhibits high activity against ethylene polymerization, but due to its heterogeneous catalytic activity, the molecular weight distribution of the resulting polymer is generally wide, and in particular, the composition distribution is not uniform in the copolymer of ethylene and α-olefin. There was this.

Recently, a so-called metallocene catalyst system has been developed, which is composed of a metallocene compound of a periodic table Group 4 transition metal such as titanium, zirconium, and hafnium and methylaluminoxane as a promoter. Since the metallocene catalyst system is a homogeneous catalyst having a single catalytic activity point, the metallocene catalyst system has a characteristic of producing polyethylene having a narrower molecular weight distribution and a uniform composition distribution than the conventional Ziegler-Natta catalyst system. For example, European Patent Nos. 320,762, 3,726,325 or JP 63-092621, JP 02-84405, or JP 03-2347 disclose Cp ₂ TiCl ₂ , Cp ₂ ZrCl ₂ , Cp ₂ ZrMeCl, Cp ₂ ZrMe ₂ , Ethylene (IndH ₄ ) ₂ ZrCl _2, etc., by activating the metallocene compound with the cocatalyst methylaluminoxane to polymerize ethylene with high activity so that the molecular weight distribution (Mw / Mn) ranges from 1.5 to 2.0. It has been announced that polyethylene can be prepared. However, it is difficult to obtain a high molecular weight polymer in the catalyst system. Especially, when applied to a solution polymerization method performed at a high temperature of 140 ° C. or higher, the polymerization activity is drastically reduced and the β-hydrogen desorption reaction is predominant, so that the weight average molecular weight is 100,000 (Mw). It is known to be inadequate for the preparation of high molecular weight polymers).

On the other hand, Exxon U.S. Patent No. 5,084,534 is a result of ethylene homopolymerization or copolymerization of ethylene with 1-hexene and 1-octene at 150-200 ° C using (n-BuCp) ₂ ZrCl ₂ catalyst and methylaluminoxane promoter It has been disclosed that a copolymer having a narrow molecular weight distribution in the range of 1.8 to 3.0 and a uniform composition distribution can be prepared. In addition, Dow's European Patent No. 0416815 and the same Patent No. 0420436 connect amide groups to one cyclopentadiene ligand in the form of a ring, which is a geometrically controlled catalyst, in addition to slurry polymerization, ethylene homopolymerization or under solution polymerization conditions. It has been disclosed that a high molecular weight polymer having high catalytic activity in copolymerization of ethylene and α-olefin and having excellent reactivity with comonomers and uniform composition distribution can be prepared. However, like the metallocene catalyst, the catalyst system also rapidly decreases the stability and copolymerization of the catalyst as the temperature increases at a high temperature solution polymerization condition of 140 ° C. or higher, and it is difficult to use commercially due to the high cost of raw materials. .

In order to overcome the problems of the prior art, the present inventors have conducted extensive research. As a result, a geometrically-bound catalyst in which a cyclopentadienyl derivative and an electron-donating substituent are substituted with an alkyl group at a 3,4-position around a Group 4 transition metal In the case of the copolymerization is significantly improved, it was found that the solution polymerization process is carried out at a high temperature of 140 ℃ or more suitable for the production of high activity and high molecular weight ethylene homopolymer or elastomeric copolymer with α-olefin, Was completed on this basis.

Accordingly, an object of the present invention is to easily prepare a single-site catalyst having excellent thermal stability and excellent copolymerizability and a copolymer of ethylene homopolymer or α-olefin having various physical properties using such catalyst components from a commercial point of view. It is to provide a high temperature solution polymerization method.

In order to achieve the above object, the present invention is characterized by a transition metal of Formula 1 below, and specifically, as a central metal, a cyclopentadiene derivative having an alkyl substituted at a 3,4-position around a Group 4 transition metal on the periodic table. It relates to a transition metal compound characterized in that the electron-donating substituent is crosslinked. Also such transition metal compounds; And a cocatalyst selected from aluminum compounds, boron compounds, or mixtures thereof, and a method for preparing an ethylene homopolymer or a copolymer of ethylene and an α-olefin using the same.

The transition metal compound of Formula 1

[Formula 1]

[In Formula 1,

M is a transition metal of Group 4 on the periodic table;

R ¹ and R ² are (C 1 -C 7) alkyl groups in the 3,4-position independently of each other in M and eta ⁵ -bondable cyclopentadienyl;

D is -O-, -S-, -N (R ⁵ )-or -P (R ⁶ )-, and R ⁵ and R ⁶ are independently of each other a hydrogen atom (C1-C20) alkyl group, (C3-C20) A cycloalkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1-C20) alkylcarbonyl group or (C3-C20) cycloalkylcarbonyl group;

R ³ And R ⁴ independently of one another is a hydrogen atom, a (C1-C20) alkyl group, a (C6-C30) aryl group, a (C6-C30) aryl (C1-C20) alkyl group, a (C1-C20) alkoxy group or a (C3-C20) ) Alkyl substituted siloxy group;

X independently of one another is a halogen atom, (C1-C20) alkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1-C20) alkoxy group, (C3-C20) alkyl Substituted siloxy group, (C1-C20) alkyl or (C6-C30) aryl Substituted amino group, (C1-C20) alkyl or (C6-C30) aryl Substituted amide group, (C1-C20) alkyl or (C6-C30) aryl A substituted phosphine group, a (C1-C20) alkyl or a (C6-C30) aryl substituted phosphido group, except that X is a cyclopentadienyl derivative;

The alkyl group, cycloalkyl group, aryl group, arylalkyl group, alkylcarbonyl group, cycloalkylcarbonyl group or alkoxy group of R ¹ , R ² , R ³ , R ⁴ , R ⁵ , R ⁶ , D and X is (C1-C20) An alkyl group, a (C3-C20) cycloalkyl group, a (C6-C30) aryl group or a (C6-C30) aryl (C10-C20) alkyl group;

n is an integer of 1 or 2.]

Another aspect of the present invention for achieving the above object is the transition metal compound; And a cocatalyst selected from an aluminum compound, a boron compound, or a mixture thereof; a ethylene homopolymer or a transition metal catalyst composition for preparing a copolymer of ethylene and an α-olefin, an ethylene homopolymer using the transition metal compound or the catalyst composition, or Copolymers of ethylene and α-olefins.

Hereinafter, the present invention will be described in more detail.

In the transition metal catalyst represented by Formula 1, M is preferably titanium, zirconium or hafnium.

In addition, R ¹ and R ² , which are (C ¹ -C 7) alkyl groups at 3,4-position independently of each other in M and η ⁵ -cyclopentadienyl, are specifically methyl, ethyl, n-propyl, It is characterized in that it is selected from isopropyl group, n-butyl group, sec -butyl group, tert -butyl group or n-pentyl group, More preferably, it is a methyl group.

The present invention provides a transition metal compound, characterized in that selected from the formula (2).

[Formula 2]

R ⁵ and R ⁶ are each independently a hydrogen atom (C1-C20) alkyl group, (C3-C20) cycloalkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1 -C20) alkylcarbonyl group or (C3-C20) cycloalkylcarbonyl group, more specifically methyl group, ethyl group, n-propyl group, isopropyl group, sec -butyl group or tert -butyl group, cyclohexyl group, dicy claw-hexyl group, an adamantyl group, a phenyl group, a phenyl group, methyl carbonyl, ethyl carbonyl group, propyl carbonyl group, n-, isopropyl carbonyl group, tert - butyl carbonyl group or adamantyl carbonyl group. The most preferable of these is a nitrogen atom or a phosphorus atom having a tert -butylcarbonyl group or adamantylcarbonyl group bonded thereto.

R ³ combined with Si in Formula 2 And R ⁴ independently of one another is a hydrogen atom, a (C1-C20) alkyl group, a (C6-C30) aryl group, a (C6-C30) aryl (C1-C20) alkyl group, a (C1-C20) alkoxy group or a (C3-C20) A) alkyl substituted siloxy group, and examples of the (C1-C20) alkyl group include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, sec -butyl group, tert -butyl group, n-pentyl group, Neopentyl group, amyl group, n-hexyl group, n-octyl group, n-decyl group, n-dodecyl group, n-pentadecyl group or n-eicosyl group, Among these, a methyl group, an ethyl group, and an isopropyl group are preferable. , tert -butyl group or amyl group; Examples of (C6-C30) aryl group or (C6-C30) aryl (C1-C20) alkyl group are benzyl group, (2-methylphenyl) methyl group, (3-methylphenyl) methyl group, (4-methylphenyl) methyl group, (2 , 3-dimethylphenyl) methyl group, (2,4-dimethylphenyl) methyl group, (2,5-dimethylphenyl) methyl group, (2,6-dimethylphenyl) methyl group, (3,4-dimethylphenyl) methyl group, (4 , 6-dimethylphenyl) methyl group, (2,3,4-trimethylphenyl) methyl group, (2,3,5-trimethylphenyl) methyl group, (2,3,6-trimethyl-phenyl) methyl group, (3,4, 5-trimethylphenyl) methyl group, (2,4,6-trimethylphenyl) methyl group, (2,3,4,5-tetramethylphenyl) methyl group, (2,3,4,6-tetramethylphenyl) methyl group, (2, 3,5,6-tetramethylphenyl) methyl group, (pentamethylphenyl) methyl group, (ethylphenyl) methyl group, (n-propylphenyl) methyl group, (isopropylphenyl) methyl group, (n-butylphenyl) methyl group, (sec-butyl Phenyl) methyl group, (tert-butylphenyl) methyl group, (n-pentylphenyl) methyl group, (neopentylphenyl) methyl group, (n-hexylphenyl) methyl group, (n-octylphenyl) methyl group, (n-decylpe Nil) methyl group, (n-dodecylphenyl) methyl group, (n-tetradecylphenyl) methyl group, naphthylmethyl group or anthracenylmethyl group, among which benzyl is preferable; Examples of the (C1-C20) alkoxy group are methoxy group, ethoxy group, n-propoxy group, isopropoxy group, n-butoxy group, sec -butoxy group, tert -butoxy group, n-pentoxy group and neopentoxy group , n-hexoxy group, n-octoxy group, n-dodecoxy group, n-pentadexyl group or n-ecosoxy group, and among these, methoxy group, ethoxy group, isopropoxy group or tert- Butoxy group; Examples of the (C3-C20) alkylsiloxy group include trimethylsiloxy group, triethylsiloxy group, tri-n-propylsiloxy group, triisopropylsiloxy group, tri-n-butylsiloxy group, tri- sec -butylsiloxy group, Tri- tert -butylsiloxy group, tri-isobutylsiloxy group, tert -butyldimethylsiloxy group, tri-n-pentylsiloxy group, tri-n-hexylsiloxy group or tricyclohexylsiloxy group, among which Preferred are trimethylsiloxy groups or tert -butyldimethylsiloxy groups.

X independently of one another is a halogen atom, (C1-C20) alkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1-C20) alkoxy group, (C3-C20) alkyl Substituted siloxy group, (C1-C20) alkyl or (C6-C30) aryl Substituted amino group, (C1-C20) alkyl or (C6-C30) aryl Substituted amide group, (C1-C20) alkyl or (C6-C30) aryl Substituted phosphine groups, (C 1 -C 20) alkyl or (C 6 -C 30) aryl substituted phosphido groups, except that X is a cyclopentadienyl derivative. Examples of the halogen atom include fluorine, chlorine, bromine or iodine atoms; Examples of the (C1-C20) alkyl group are methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, sec -butyl group, tert -butyl group, n-pentyl group, neopentyl group, amyl group, n -Hexyl group, n-octyl group, n-decyl group, n-dodecyl group, n-pentadecyl group or n-eicosyl group, of which methyl, ethyl, isopropyl, tert -butyl or amyl Is; Examples of the (C6-C30) aryl (C1-C20) alkyl group are benzyl group, (2-methylphenyl) methyl group, (3-methylphenyl) methyl group, (4-methylphenyl) methyl group, (2,3-dimethylphenyl) methyl group, (2,4-dimethylphenyl) methyl group, (2,5-dimethylphenyl) methyl group, (2,6-dimethylphenyl) methyl group, (3,4-dimethylphenyl) methyl group, (4,6-dimethylphenyl) methyl group, (2,3,4-trimethylphenyl) methyl group, (2,3,5-trimethylphenyl) methyl group, (2,3,6-trimethyl-phenyl) methyl group, (3,4,5-trimethylphenyl) methyl group, ( 2,4,6-trimethylphenyl) methyl group, (2,3,4,5-tetramethylphenyl) methyl group, (2,3,4,6-tetramethylphenyl) methyl group, (2,3,5,6-tetramethylphenyl ) Methyl group, (pentamethylphenyl) methyl group, (ethylphenyl) methyl group, (n-propylphenyl) methyl group, (isopropylphenyl) methyl group, (n-butylphenyl) methyl group, (sec-butylphenyl) methyl group, (tert-butyl Phenyl) methyl group, (n-pentylphenyl) methyl group, (neopentylphenyl) methyl group, (n-hexylphenyl) methyl group, (n-octylphenyl) methyl group, (n-decylphenyl) methyl group, (n-decyl Carbonyl) methyl group, (n- tetradecyl phenyl) methyl group, can be mentioned a naphthyl group or an anthracenyl group, of which preferred is a benzyl group; Examples of the (C1-C20) alkoxy group are methoxy group, ethoxy group, n-propoxy group, isopropoxy group, n-butoxy group, sec -butoxy group, tert -butoxy group, n-pentoxy group and neopentoxy group , n-hexoxy group, n-octoxy group, n-dodecoxy group, n-pentadexyl group or n-ecosoxy group, and among these, methoxy group, ethoxy group, isopropoxy group or tert- Butoxy group; Examples of the (C3-C20) alkyl substituted siloxy group are trimethylsiloxy group, triethylsiloxy group, tri-n-propylsiloxy group, triisopropylsiloxy group, tri-n-butylsiloxy group, tri- sec -butylsiloxy group And tri- tert -butylsiloxy group, tri-isobutylsiloxy group, tert -butyldimethylsiloxy group, tri-n-pentylsiloxy group, tri-n-hexylsiloxy group or tricyclohexylsiloxy group, Preferred are trimethylsiloxy groups or tert -butyldimethylsiloxy groups; Examples of the (C1-C20) alkyl or (C6-C30) allyl substituted amino group are dimethylamino group, diethylamino group, di-n-propylamino group, diisopropylamino group, di-n-butylamino group, di- sec -butyl Amino group, di- tert -butylamino group, diisobutylamino group, tert - butylisopropylamino group, di-n-hexylamino group, di-n-octylamino group, di-n-decylamino group, diphenylamino group, dibenzylamino group, Methylethylamino group, methylphenylamino group, benzylhexylamino group, bistrimethylsilylamino group or bis-tert-butyldimethylsilylamino group, among which preferred is a dimethylamino group or diethylamino group; Examples of the (C1-C20) alkyl or (C6-C30) aryl substituted amide group are dibenzylamide group, methylethylamide group, methylphenylamide or benzylhexylamide group, bistrimethylsilylamino group, of which diphenyl is preferable. An amide group; Examples of the (C1-C20) alkyl or (C6-C30) allyl substituted phosphine group include dimethylphosphine group, diethylphosphine group, di-n-propylphosphine group, diisopropylphosphine group, di-n-butylphosphine group , Di- sec -butylphosphine group, di- tert -butylphosphine group, diisobutylphosphine group, tert -butylisopropylphosphine group, di-n-hexylphosphine group, di-n-octylphosphine group, di-n -A decylphosphine group, diphenylphosphine group, dibenzylphosphine group, methylethylphosphine group, methylphenylphosphine group, benzylhexylphosphine group, bistrimethylsilylphosphine group or bis-tert-butyldimethylsilylphosphine group; Examples of the (C1-C20) alkyl or (C6-C30) aryl-substituted phosphido group are dibenzylphosphido group, methylethylphosphido group, methylphenylphosphido group or benzylhexylphosphido group, bistrimethylsilylphosphido group to be.

N in the formula (2) is an integer of 1 to 4 selected by the oxidation value of the transition metal, preferably an integer of 1 or 2.

The present invention relates to an ethylene homopolymer or a copolymer of ethylene and an α-olefin prepared using the transition metal compound according to the above as a catalyst.

On the other hand, the transition metal compound of the formula (1) is a counter ion having a weak binding force while extracting the X ligand in the transition metal compound according to the present invention to be the active catalyst component used in the olefin polymerization, while cationizing the central metal That is, boron compounds, aluminum compounds or mixtures thereof that can act as anions are used as promoters. At this time, the aluminum compound used is to remove traces of polar substances acting as a catalyst poison such as water, but may act as an alkylating agent when the X ligand is halogen.

The boron compound used as a promoter in the present invention may be selected from compounds represented by the following Chemical Formula 3, Chemical Formula 4 or Chemical Formula 5 as shown in US Patent No. 5,198,401.

(3)

B (R ⁷ ) ₃

[Formula 4]

[R ⁸ ] ⁺ [B (R ⁷ ) ₄ ] ^-

[Chemical Formula 5]

[(R ⁹ ) _q ZH] ⁺ [B (R ⁷ ) ₄ ] ^-

In Chemical Formulas 3 to 5, B is a boron atom; R ⁷ is a phenyl group, wherein the phenyl group is 3 to 5 selected from a fluorine atom, a (C1-C20) alkyl group unsubstituted or substituted by a fluorine atom, or a (C1-C20) alkoxy group unsubstituted or substituted by a fluorine atom May be further substituted with 4 substituents; R ⁸ is a (C5-C7) cycloalkyl radical or a (C1-C20) alkyl (C6-C20) aryl radical, a (C6-C30) aryl (C1-C20) alkyl radical such as a triphenylmethyl radical; Z is nitrogen or personnel; R ⁹ is an anilnium radical substituted with two (C 1 -C 4) alkyl groups together with a (C 1 -C 20) alkyl radical or a nitrogen atom; q is an integer of 2 or 3.

Preferred examples of the boron-based cocatalysts include tris (pentafluorophenyl) borane, tris (2,3,5,6-tetrafluorophenyl) borane, tris (2,3,4,5-tetrafluoro Phenyl) borane, tris (3,4,5-trifluorophenyl) borane, tris (2,3,4-trifluorophenyl) borane, phenylbis (pentafluorophenyl) borane, tetrakis (Pentafluorophenyl) borate, tetrakis (2,3,5,6-tetrafluorophenyl) borate, tetrakis (2,3,4,5-tetrafluorophenyl) borate, tetrakis (3,4 , 5-tetrafluorophenyl) borate, tetrakis (2,2,4-trifluorophenyl) borate, phenylbis (pentafluorophenyl) borate or tetrakis (3,5-bistrifluoromethylphenyl) borate And one or more cocatalysts selected from the above, and specific examples thereof include ferrocenium tetrakis (pentafluorophenyl) borate and 1,1'-dimethylferrocenium. Tetrakis (pentafluorophenyl) borate, silver Tetrakis (pentafluorophenyl) borate, triphenylmethyl tetrakis (pentafluorophenyl) borate, triphenylmethyl tetrakis (3,5-bistrifluoromethylphenyl) Borate, triethylammonium tetrakis (pentafluorophenyl) borate, tripropylammonium tetrakis (pentafluorophenyl) borate, tri (n-butyl) ammonium tetrakis (pentafluorophenyl) borate, tri (n-butyl Ammonium tetrakis (3,5-bistrifluoromethylphenyl) borate, N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate, N, N-diethylanilinium tetrakis (pentafluorophenyl) Borate, N, N-2,4,6-pentamethylanilinium tetrakis (pentafluorophenyl) borate, N, N-dimethylanilinium tetrakis (3,5-bistrifluoromethylphenyl) borate, diiso Propylammonium tetra S (pentafluorophenyl) borate, dicyclohexylammonium tetrakis (pentafluorophenyl) borate, triphenylphosphonium tetrakis (pentafluorophenyl) borate, tri (methylphenyl) phosphonium tetrakis (pentafluorophenyl ) Borate or tri (dimethylphenyl) phosphonium tetrakis (pentafluorophenyl) borate, the most preferred of which is N, N-dimethylanilinium tetrakispentafluorophenylborate, triphenylmethyllinium tetrakis Pentafluorophenylborate or trispentafluoroborate.

As the aluminum compound used in the present invention, an aluminoxane compound of Formula 6 or 7, an organoaluminum compound of Formula 8, or an organoaluminum hydrocarbyl oxide compound of Formula 9 or Formula 10 may be used.

[Formula 6]

(-Al (R ¹⁰ ) -O-) _m

[Formula 7]

(R ¹⁰ ) ₂ Al-(-O (R ¹⁰ )-) _p- (R ¹⁰ ) ₂

[Formula 8]

(R ¹¹ ) _r Al (E) _3-r

[Formula 9]

(R ¹² ) ₂ AlOR ¹³

[Formula 10]

R ¹² Al (OR ¹³ ) ₂

In Formulas 6 to 10, R ¹⁰ is a linear or nonlinear (C1-C20) alkyl group, preferably a methyl group or an isobutyl group, m and p are each independently an integer of 5 to 20; R ¹¹ and R ¹² are a (C1-C20) alkyl group; E is a hydrogen atom or a halogen atom; r is an integer of 1 to 3; R ¹³ may be selected from a (C1-C20) alkyl group or a (C6-C30) aryl group.

The aluminum compound is at least one cocatalyst selected from aluminoxane and organoaluminum, the aluminoxane compound being methylaluminoxane, improved methylaluminoxane or tetraisobutylaluminoxane; The organoaluminum compound is characterized in that it is selected from trialkylaluminum, dialkylaluminum chloride, alkylaluminum dichloride or dialkylaluminum hydride. Trialkylaluminum including trimethylaluminum, triethylaluminum, tripropylaluminum, triisobutylaluminum and trihexylaluminum as specific examples of the organoaluminum compound; Dialkylaluminum chlorides including dimethylaluminum chloride, diethylaluminum chloride, dipropylaluminum chloride, diisobutylaluminum chloride and dihexylaluminum chloride; Alkylaluminum dichlorides including methylaluminum dichloride, ethylaluminum dichloride, propylaluminum dichloride, isobutylaluminum dichloride and hexylaluminum dichloride; And dialkyl aluminum hydrides including dimethyl aluminum hydride, diethyl aluminum hydride, dipropyl aluminum hydride, diisobutyl aluminum hydride and dihexyl aluminum hydride. Preferably, they are triethyl aluminum and triisobutyl aluminum, and the molar ratio of a center transition metal (M): aluminum compound is 1: 50-5,000.

In addition, the ratio of the transition metal compound and the promoter is 1: 0.1 to 100: 10 to 1,000, more preferably 1: 0.5 to 5: 25 to the molar ratio of the center transition metal (M): boron compound: aluminum compound. 500. In this ratio, it is possible to prepare an ethylene homopolymer or a copolymer of ethylene and an α-olefin, and the range of the ratio varies depending on the purity of the reaction.

Another aspect of the present invention relates to an ethylene homopolymer or a copolymer of ethylene and an α-olefin prepared using the transition metal compound as a catalyst composition. The catalyst and the ethylene or α-olefin comonomers are contacted to proceed in solution. In this case, the transition metal compound and the cocatalyst component may be separately added to the reactor, or each component may be previously mixed and added to the reactor.

Preferred organic solvents that can be used in the preparation method are (C3-C20) hydrocarbons, specific examples of which are butane, isobutane, pentane, hexane, heptane, octane, isooctane, nonane, decane, dodecane, cyclohexane, methylcyclo Hexane, benzene, toluene and xylene.

Specifically, in the production of ethylene homopolymer, ethylene is used alone as a monomer, and the pressure of ethylene suitable for the present invention is 1 to 1000 atm and more preferably 10 to 150 atm. When the pressure is in the above range, the material of the reactor is thinner and there is no need to undergo an additional compression process, thereby improving economic efficiency and improving the yield of the polymer . Moreover, polymerization temperature is between 60 degreeC-300 degreeC, Preferably it is 80 degreeC-250 degreeC. If the polymerization temperature is 80 ℃ or more can improve the copolymerization can be produced low-density polymer, and below 250 ℃ the conversion rate of ethylene to the polymer is improved to obtain a high-density polymer.

In the method for preparing ethylene homopolymer or copolymer of ethylene and α-olefin using a transition metal catalyst composition, α-olefin of (C3-C18) hydrocarbon may be used as the comonomer polymerized with ethylene. Propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1 -Hexadecene, 1-octadecene and 1-aitocene. More preferably, 1-butene, 1-hexene, 1-octene, or 1-decene may be copolymerized with ethylene. In this case, the pressure and polymerization temperature of the preferred ethylene are the same as the preparation of the high density polyethylene, the ethylene copolymer prepared according to the method of the present invention contains at least 50% by weight of ethylene, preferably at least 60% by weight, more Preferably from 60% to 99% by weight of ethylene. As described above, linear low density polyethylene (LLDPE) prepared using α-olefin of (C4-C10) hydrocarbon as comonomer has a density range of 0.850 to 0.950 g / cc, preferably 0.860 to 0.940 g / The production of cc olefin copolymers is possible.

Hydrogen may be used as a molecular weight regulator to control the molecular weight in the preparation of the ethylene homopolymer or copolymer according to the present invention, and has a weight average molecular weight (Mw) in the range of 80,000 to 500,000, as a weight average molecular weight / number average molecular weight It has a molecular weight distribution (Mw / Mn) in the range of 1.5 to 4.1.

Since the catalyst composition presented in the present invention is present in a uniform form in the polymerization reactor, it is preferable to apply to the solution polymerization process carried out at a temperature above the melting point of the polymer. However, as disclosed in US Pat. No. 4,752,597, the transition metal compound and the co-catalyst may be supported on a porous metal oxide support, which may be used in slurry polymerization or gas phase polymerization as a heterogeneous catalyst system.

The transition metal compound or the catalyst composition including the transition metal compound according to the present invention is produced in a simple and high yield, and is easily manufactured in an economical manner by reducing the number of alkyls, leaving only a specific portion of cyclopentadiene. In addition, the thermal stability of the catalyst is excellent, high molecular weight polymer can be produced in high yield while maintaining high catalytic activity in olefin polymerization carried out under high temperature solution polymerization conditions, and the copolymerization reactivity with α-olefin Because of its superior commercial viability compared to known metallocene and nonmetallocene-based single active catalysts.

Therefore, the transition metal catalyst composition and the preparation method according to the present invention can be usefully used for preparing a copolymer of ethylene and a-olefin having various physical properties and elasticity.

Hereinafter, the present invention will be described in detail with reference to Examples, but the scope of the present invention is not limited by the following Examples.

Except where noted, all ligand and catalyst synthesis experiments were performed using standard Schlenk or glovebox techniques under nitrogen atmosphere and the organic solvent used in the reaction was refluxed under sodium metal and benzophenone to remove moisture Distilled immediately before use. ¹ H-NMR analysis of the synthesized ligand and catalyst was performed using a Bruker 500 MHz spectrometer at room temperature.

Cyclohexane, a polymerization solvent, was used after passing through a tube filled with Q-5 catalyst (BASF Co.), silica gel and activated alumina and bubbling with high purity nitrogen to remove moisture, oxygen and other catalyst poisons. .

The polymerized polymer was analyzed by the method described below.

1. Melt Flow Index (MI)

It measured according to ASTM D 2839.

2. Density

According to ASTM D 1505, it was measured using a density gradient tube.

3. Melting Point (Tm) Analysis

Dupont DSC2910 was used in a 2 ^nd heating conditions at a rate of 10 ° / min under a nitrogen atmosphere.

4. Molecular Weight and Molecular Weight Distribution

PL210 GPC equipped with PL Mixed-BX2 + preCol was measured at 135 ° C. at a rate of 1.0 mL / min in 1,2,3-trichlorobenzene solvent and molecular weight was corrected using PL polystyrene standards.

5. a-olefin content (% by weight) in the copolymer

The Bruker DRX500 nuclear magnetic resonance spectrometer was used to measure ¹³ C-NMR mode at 120 ° C. using a 1,2,4 trichlorobenzene / C ₆ D ₆ (7/3 weight fraction) mixed solvent at 125 MHz.

(Reference: Randal, JC JMS - Rev . Macromol . Chem . Phys . 1980 , C29 , 201)

Preparation Example 1 Synthesis of ( dichloro ) ( tert - butylamido ) (3,4- dimethylcyclopentadienyl ) ( dimethylsilane ) titanium ( IV )

(1) Synthesis of Isopropyl Ester Crotonic Acid

Dissolve crotonic acid (193.7 g, 2.25 mol) in a 2 L flask containing 2-propanol (860 mL, 11.25 mol), stir well, and add sulfuric acid (24 mL, 0.45 mol) slowly to the mixture to reflux and stir for at least 48 hours. Let's do it. After cooling to room temperature, the resulting mixture was washed with 1000 mL of distilled water, and the organic layer was separated, neutralized and distilled under normal pressure (80 ^° C.) to obtain 220 g (1.71 mol, yield 76.3%) of isopropyl ester crotonic acid.

¹ H-NMR (C ₆ D ₆ ) δ = 1.01 to 1.06 (d, 6H), 1.26 to 1.37 (q, 3H), 5.01 to 5.08 (m, 1H), 5.70 to 5.79 (m, 1H), 6.82 to 6.93 (m, 1H) ppm

(2) Synthesis of 3,4-dimethyl-2-cyclopentenone

1 L of polyphosphoric acid is placed in a 2 L flask, nitrogen-substituted, and isopropyl ester crotonic acid (76.9 g, 0.6 mol) is slowly added dropwise while stirring and refluxing at 100 ^° C. for about 3 hours to turn dark brown. The resulting mixture was mixed with 500 mL of ice water, neutralized with sodium carbonate, extracted with ethyl ether, and then distilled under reduced pressure (105 ^o C, 40 Torr) to give 56 g (0.51) of colorless and transparent liquid 3,4-dimethyl-2-cyclopentenone. mol, yield 84.7%).

¹ H-NMR (CDCl ₃ ) δ = 1.05 to 1.09 (d, 3H), 1.83 to 1.87 (q, 1H), 1.98 (s, 3H), 2.45 to 2.51 (q, 1H), 2.67 to 2.70 (m, 1H), 5.73 (s, 1H) ppm

(3) tert-butyl-1- (3,4-dimethylcyclopentadienyl) -1,1-dimethylsilaneamine

6.07 g (0.16 mol) of lithium aluminum hydride was dissolved in 250 mL of diethyl ether in nitrogen, and 33.95 g (0.31 mol) of 3,4-dimethyl-2-cyclopentenone was slowly added dropwise at 0 ° C. The mixture was refluxed for 30 minutes, lowered to 0 ° C. through room temperature, and 15 mL of distilled water was slowly added dropwise to remove unreacted lithium aluminum hydride. The reaction mixture was slowly poured into dilute sulfuric acid, and the organic layer was extracted with diethyl ether, followed by distillation under reduced pressure to obtain 21.2 g of 2,3-dimethylcyclopentadiene as a yellow liquid component. Transfer the solution to a flask, dissolve in 200 mL of pentane, lower the temperature to -78 ° C, and add 141 mL (0.225 mol, 1.6 M) of n-butyllithium dropwise. After raising to room temperature and reacting for 12 hours, 10.5 g (yield 46.9%) of 1,2-dimethylcyclopentadienyl lithium in the form of an off-white powder was obtained. 5.45 g (54.5 mmol) of the powder was added to a flask containing 80 mL of diethyl ether, and the temperature was lowered to −78 ° C., and 6.8 mL (54.5 mmol) of dichlorodimethylsilane was added dropwise. The temperature is raised to room temperature and reacted for at least 12 hours. Removal of diethyl ether by distillation under reduced pressure and washing with pentane yielded 6.35 g (yield 62.4%) of dimethylsilyl-3,4-dimethylcyclopentadienyl chloride as a yellow liquid. Transfer the liquid to the flask without purification, dissolve in 90 mL of tetrahydrofuran, and slowly add dropwise 2.69 g (34.0 mmol) of lithium tert -butylamine at -78 ° C. After the reaction at room temperature for 12 hours or more, the solvents were all removed by vacuum drying, and extracted with purified pentane to give tert -butyl-1- (3,4-dimethylcyclopentadienyl) -1,1-dimethylsilane as a yellow liquid. 6.15 g (27.5 mmol, yield 80.9%) of amine were obtained.

¹ H NMR (C ₆ D ₆ ): δ = 0.00 (s, 6H), 0.28 (s, 3H), 1.05 (s, 3H), 1.07 (s, 9H), 1.09 (s, 3H), 1.85 (s , 2H), 1.94 (s, 2H), 1.98 (s, 6H), 2.89 (t, 1H), 3.17 (t, 1H), 6.16 (s, 2H), 6.31-6.70 (m, 1H) ppm

(4) Synthesis of (dichloro) ( tert -butylamido) (3,4-dimethylcyclopentadienyl) (dimethylsilane) titanium (IV)

6.15 g (27.5 mmol) of tert -butyl-1- (3,4-dimethylcyclopentadienyl) -1,1-dimethylsilaneamine was dissolved in a flask and dissolved in 100 mL of diethyl ether under nitrogen, followed by n at -78 ° C. Slowly add 22.0 mL of butyllithium dropwise. Slowly raise the temperature to room temperature and react for 12 hours or more. The solvent was removed by vacuum drying and washed with pentane to obtain 5.24 g (yield 81.0%) of an off-white powder of lithium ( tert -butylamido) (3,4-dimethylcyclopentadienyl) dimethylsilane. 3.00 g (12.8 mmol) and 4.26 g (12.8 mmol) of tetrachlorobis (tetrahydrofuran) titanium (IV) are put together in a flask, and 50 mL of toluene is added thereto and reacted at 80 ° C. for at least 24 hours. The mixture was cooled to room temperature, filtered to remove lithium chloride, the solvent was removed by vacuum drying, extracted with pentane and recrystallized to give (dichloro) ( tert -butylamido) (3,4-dimethylcyclopentadienyl as a yellow solid). ) (Dimethylsilane) titanium (IV) 1.73 g (yield 39.9%) were obtained.

¹ H NMR (C ₆ D ₆ ): δ = 0.26 (s, 6H), 1.40 (s, 9H), 2.04 (s, 6H), 5.91 (s, 2H) ppm; ¹³ C NMR (C ₆ D ₆ ): δ = 0.97, 13.41, 33.18, 105.91, 123.05, 127.84, 128.22, 133.45 ppm.

Preparation Example 2 Synthesis of ( Dichloro ) ( tert - butylamido ) (3,4- dimethylcyclopentadienyl ) ( dimethylsilane ) zirconium ( IV )

In a flask, 0.9 g (3.83 mmol) of lithium ( tert -butylamido) 3,4-dimethylcyclopentadienyldimethylsilane and 0.891 g (3.83 mmol) of zirconium (IV) chloride were added together in a flask, and 20 mL of toluene was added thereto. The reaction is carried out for at least 24 hours. The mixture was cooled to room temperature, filtered to remove lithium chloride, the solvent was removed by vacuum drying, extracted with pentane and recrystallized to give (dichloro) ( tert -butylamido) (3,4-dimethylcyclopentadier) as a light brown solid. Nil) (dimethylsilane) zirconium (IV) 0.89g (yield 60.5%) was obtained.

¹ H NMR (C ₆ D ₆ ): δ = 0.30 (s, 6H), 1.31 (s, 9H), 2.00 (s, 6H), 5.90 (s, 2H) ppm; ¹³ C NMR (C ₆ D ₆ ): δ = 0.07, 14.36, 32.65, 107.74, 126.86, 126.91, 128.82, 139.34 ppm.

Comparative Preparation Example 1 Synthesis of ( dichloro ) ((dimethyl) ( tert - butylamino ) (2,3,4,5- tetramethylcyclopentadienyl ) silyl) titanium ( IV )

(1) Synthesis of (dimethyl) ( tert -butylamido) (2,3,4,5-tetramethylcyclopenta-2,4-dienyl) silane

2,3,4,5-tetramethylcyclopenta-2,4-diene (3.67g, 30mmol) was added to a flask containing 100mL of tetrahydrofuran, and n-butyllithium (12mL) was added dropwise at 0 ° C. The reaction was carried out for 8 hours at room temperature. The solution was cooled to -78 ° C and slowly added dropwise dichlorodimethylsilane (3.87g, 30mmol) and reacted for 12 hours. After the reaction, the volatiles were removed, extracted with 100 mL of hexane, and the volatiles were removed to obtain 5.5 g of (chloro) (dimethyl) (2,3,4,5-tetramethylcyclopentadienyl) silane of light yellow oil. The resulting (chloro) (dimethyl) (2,3,4,5-tetramethylcyclopentadienyl) silane was dissolved in 100 mL of tetrahydrofuran without further purification, and then lithium tert-butylamide (2.02 g) was dissolved at 0 ° C. The reaction mixture was added dropwise at to react at room temperature for 2 hours. After the reaction, the volatiles were removed, extracted with 100 mL of hexane, 6.09 g of (dimethyl) ( tert -butylamido) (2,3,4,5-tetramethylcyclopenta-2,4-dienyl) silane of light yellow oil. (Yield 81%) was obtained.

¹ H-NMR (C ₆ D ₆ ) δ = 0.11 (s, 6H), 1.11 (s, 9H), 1.86 (s, 6H), 2.00 (s, 6H) 2.78 (s, 1H) ppm

(2) Synthesis of (dichloro) ((dimethyl) ( tert -butylamino) (2,3,4,5-tetramethylcyclopentadienyl) silyl) titanium (IV)

(tert-butylamido) (2,3,4,5-tetramethylcyclopenta-2,4-dienyl) dimethylsilane (6.09 g 24.2 mmol) was dissolved in 100 mL of diethyl ether and then n at -78 ° C. -Butyl lithium (9.7 mL) was added dropwise and slowly raised to room temperature to react for 12 hours. After the reaction, the volatiles were removed and extracted with 100 mL of hexane to give 6.25 g of an orange solid component. The obtained solid was dissolved in 100 mL of toluene, tetrachlorotitanium (IV) (4.50 g 23.7 mmol) was added dropwise at -78 ° C, and the reaction mixture was heated to room temperature for 7 hours. After completion of the reaction, the volatiles were removed, extracted with purified 100 mL of pentane, recrystallized at -35 ° C., filtered and dried under reduced pressure to give (dichloro) ((dimethyl) (tert-butylamino) (2, 0.87 g (yield 10%) of 3,4,5-tetramethylcyclopentadienyl) silyl) titanium (IV) were obtained.

¹ H-NMR (C ₆ D ₆ ) δ = 0.43 (s, 6H), 1.43 (s, 9H), 2.00 (s, 6H), 2.01 (s, 6H) ppm

Comparative Preparation Example 2 Synthesis of ( dichloro ) ((dimethyl) ( tert - butylamino ) (2,3,4,5- tetramethylcyclopentadienyl ) silyl) zirconium ( IV )

(Dichloro) ((dimethyl) (tert-butylamino) (2,3,4,5-) was synthesized in the same manner as in Comparative Preparation Example 1, except that 5.52 g (23.7 mmol) of tetrachlorozirconium (IV) was used. 1.3 g (yield 13.3%) of tetramethylcyclopentadienyl) silyl) zirconium (IV) were obtained.

¹ H-NMR (C ₆ D ₆ ) delta = 0.40 (s, 6H), 1.40 (s, 9H), 1.97 (s, 6H), 2.00 (s, 6H) ppm.

Example 1

Copolymerization of ethylene and 1-octene was carried out using a batch polymerization apparatus as follows. After sufficiently drying, 1170 mL of cyclohexane and 30 mL of 1-octene were added to a 2000 mL capacity stainless steel reactor substituted with nitrogen, and then modified methylaluminoxane-7 (Akzo Nobel, modified MAO-7, 7 wt% Al Isopar solution) 54.2 mM 22.1 mL of toluene solution was added to the reactor. The reactor was then heated to 80 ° C. and then synthesized in Preparation Example 1 (dichloro) ( tert -butylamido) (3,4-dimethylcyclopentadienyl) (dimethylsilane) titanium (IV) (5.0 mM toluene Solution) 0.4 mL of triphenylmethyllinium tetrakis pentafluorophenylborate (99%, Boulder Scientific) 10 mL of toluene solution was added sequentially, followed by filling the reactor with ethylene to 30 kg / cm ² and continuously It was fed to allow polymerization. The reaction time was reached to a maximum temperature of 162.2 ° C. for 5 minutes, and after 5 minutes, ethanol containing 100 mL of 10 vol% aqueous hydrochloric acid solution was added to terminate the polymerization. After stirring for 1 hour with 1.5 L of ethanol, the reaction product was filtered, Separated. The recovered reaction product was dried in a vacuum oven at 60 ° C. for 8 hours, yielding 62.8 g of a polymer. The melting point of the polymer was 117.48 ℃, the melt index was 0.016, the density was 0.9124 g / cc, the weight average molecular weight (Mw) was 202,000 g / mol and the molecular weight distribution (Mw / Mn) was 4.05 when analyzed by gel chromatography. , 1-octene content was 7.68% by weight.

[Example 2]

Copolymerization of ethylene and 1-octene was carried out in the same manner as in Example 1 except that the reaction temperature before the catalyst was heated to 140 ° C. The reaction time reached a maximum temperature of 180.9 ° C. for 5 minutes and finally gave 48.04 g of a polymer. The melting point of the polymer was 119.02 ℃, the melt index was 1.5 and the density was 0.9152 g / cc. The weight average molecular weight (Mw) was 109,100 g / mol and the molecular weight distribution (Mw / Mn) was 2.33 when analyzed by gel chromatography. The 1-octene content was 4.98 wt%.

Example 3

0.4 mL of (dichloro) (tert-butylamido) (3,4-dimethylcyclopentadienyl) (dimethylsilane) zirconium (IV) (5.0 mM toluene solution) synthesized in Preparation Example 2 was added. Copolymerization of ethylene and 1-octene was carried out in the same manner as in Example 1 except that 10 minutes were observed. The reaction time reached a maximum temperature of 98.2 ° C. for 10 minutes and finally 4.62 g of polymer was obtained. The melting point of the polymer was 133.28 ℃, the melt index was 0.165, and the density was 0.9370g / cc. The weight average molecular weight (Mw) was 211,600g / mol and the molecular weight distribution (Mw / Mn) was 3.13 when analyzed by gel chromatography. , 1-octene content was 0.82% by weight.

Comparative Example 1

Synthesized in Comparative Production Example 1 (Dichloro) ((dimethyl) ( tert -butylamino) (2,3,4,5-tetramethylcyclopentadienyl) silyl) titanium (IV) was used in the same manner as in Example 1 except that Copolymerization with 1-octene was performed. The reaction time reached a maximum temperature of 163.0 ° C. for 5 minutes and finally 66.68 g of a polymer was obtained. The melting point of the polymer was 116.35 ℃, the melt index was 0.004, the density was 0.9420 g / cc, the weight average molecular weight (Mw) was 247,800 g / mol and the molecular weight distribution (Mw / Mn) was 7.30 when analyzed by gel chromatography. , 1-octene content was 6.55% by weight.

Comparative Example 2

(Dichloro) ((dimethyl) (( tert -butylamino) (2,3,4,5-tetramethylcyclopentadienyl) silyl) synthesized in Comparative Preparation Example 1 by heating the reaction temperature before adding the catalyst to 140 ° C Copolymerization of ethylene and 1-octene was carried out in the same manner as in Example 1 except that titanium (IV) was used. The reaction time reached a maximum temperature of 184.4 ° C. for 5 minutes and finally 40.03 g of a polymer was obtained. The melting point of the polymer was 116.21 ℃, the melt index was 0.56, the density was 0.9218g / cc, the weight average molecular weight (Mw) was 106,000g / mol and the molecular weight distribution (Mw / Mn) was 4.31 when analyzed by gel chromatography. , 1-octene content of 6.34% by weight.

Comparative Example 3

0.4 mL of (dichloro) ((dimethyl) ( tert -butylamino) (2,3,4,5-tetramethylcyclopentadienyl) silyl) zirconium (IV) (5.0 mM toluene solution) synthesized in Comparative Preparation Example 2 The copolymerization of ethylene and 1-octene was carried out in the same manner as in Example 1, except that was added and the reaction time was observed for 10 minutes. The reaction time was reached to a maximum temperature of 102.1 ℃ for 10 minutes to finally obtain a polymer of 16.49g. Melting point of the polymer was 125.93 ℃, melt index was 0.087, density was 0.9405 g / cc, and the weight average molecular weight (Mw) was 426,800 g / mol and molecular weight distribution (Mw / Mn) was 3.31 when analyzed by gel chromatography. , 1-octene content was 2.2% by weight.

As can be seen from the above examples, an olefin copolymer having a higher polymer yield and a higher 1-octene content under the same conditions in the polymerization conditions of ethylene homopolymerization and 1-octene was prepared. Can be. In particular, low density copolymers were successfully obtained with ethylene and 1-octene.

Although described in detail with respect to embodiments of the present invention as described above, those of ordinary skill in the art, without departing from the spirit and scope of the invention as defined in the appended claims Various modifications may be made to the invention. Therefore, modifications of the embodiments of the present invention will not depart from the scope of the present invention.

Claims (13)

The transition metal compound of Formula 1
[Formula 1]

[In the above formula (1)
M is a transition metal of Group 4 on the periodic table;
R ¹ and R ² are (C 1 -C 7) alkyl groups in the 3,4-position independently of each other in M and eta ⁵ -bondable cyclopentadienyl;
D is -O-, -S-, -N (R ⁵ )-or -P (R ⁶ )-, and R ⁵ and R ⁶ are independently of each other a hydrogen atom (C1-C20) alkyl group, (C3-C20) A cycloalkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1-C20) alkylcarbonyl group or (C3-C20) cycloalkylcarbonyl group;
R ³ And R ⁴ independently of one another is a hydrogen atom, a (C1-C20) alkyl group, a (C6-C30) aryl group, a (C6-C30) aryl (C1-C20) alkyl group, a (C1-C20) alkoxy group or a (C3-C20) ) Alkyl substituted siloxy group;
X independently of one another is a halogen atom, (C1-C20) alkyl group, (C6-C30) aryl group, (C6-C30) aryl (C1-C20) alkyl group, (C1-C20) alkoxy group, (C3-C20) alkyl Substituted siloxy group, (C1-C20) alkyl or (C6-C30) aryl Substituted amino group, (C1-C20) alkyl or (C6-C30) aryl Substituted amide group, (C1-C20) alkyl or (C6-C30) aryl A substituted phosphine group, a (C1-C20) alkyl or a (C6-C30) aryl substituted phosphido group, except that X is a cyclopentadienyl derivative;
The alkyl group, cycloalkyl group, aryl group, arylalkyl group, alkylcarbonyl group, cycloalkylcarbonyl group or alkoxy group of R ¹ , R ² , R ³ , R ⁴ , R ⁵ , R ⁶ , D and X is (C1-C20) An alkyl group, a (C3-C20) cycloalkyl group, a (C6-C30) aryl group or a (C6-C30) aryl (C10-C20) alkyl group;
n is an integer of 1 or 2.] The method of claim 1,
M is a transition metal compound, characterized in that titanium, zirconium or hafnium. The method of claim 1,
R ¹ and R ² are independently selected from methyl, ethyl, n-propyl, isopropyl, n-butyl, sec-butyl, tert-butyl or n-pentyl. Metal compounds. The method of claim 1,
R ⁵ and R ⁶ are each independently a methyl group, ethyl group, n-propyl group, isopropyl group, sec -butyl group or tert -butyl group, cyclohexyl group, dicyclohexylmethyl group, adamantyl group, phenyl group and phenylmethyl group Transition metal compound, characterized in that selected from methylcarbonyl group, ethylcarbonyl group, n-propylcarbonyl group, isopropylcarbonyl group, tert -butylcarbonyl group or adamantylcarbonyl group. The transition metal compound according to any one of claims 1 to 4; And a promoter selected from an aluminum compound, a boron compound, or a mixture thereof. The transition metal catalyst composition for preparing a copolymer of ethylene homopolymer or α-olefin. The method of claim 5,
The aluminum compound is a cocatalyst selected from aluminoxanes and organoaluminum, and may be methylaluminoxane, improved methylaluminoxane, tetraisobutylaluminoxane, trialkylaluminum, dialkylaluminum chloride, alkylaluminum dichloride, dialkylaluminum. Selected from hydrides or mixtures thereof; The boron compound cocatalyst is selected from N, N-dimethylanilinium tetrakispentafluorophenylborate, triphenylmethyllinium tetrakispentafluorophenylborate or mixtures thereof. Transition metal catalyst composition for preparing copolymer of -olefin. The method of claim 5,
A transition metal catalyst for preparing an ethylene homopolymer or a copolymer of ethylene and an α-olefin, wherein the ratio of the transition metal compound and the promoter is 1:50 to 5,000 based on the molar ratio of the transition metal (M) to the aluminum compound. Composition. The method of claim 5,
Ethylene homopolymer or ethylene and α-olefin, characterized in that the ratio of the transition metal compound and the promoter is used as 1: 0.5 to 5: 25 to 500 based on the molar ratio of the transition metal (M): boron compound: aluminum compound. Transition metal catalyst composition for the production of copolymers. In the method for producing an ethylene homopolymer or a copolymer of ethylene and α-olefin using the transition metal catalyst composition according to claim 5,
The comonomer polymerized with ethylene is propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1 Ethylene homopolymer or copolymer of ethylene and α-olefin, characterized in that at least one selected from hexadecene and 1-atocene, and the ethylene content in the copolymer of ethylene and the α-olefin is 50% by weight or more. Way. 10. The method of claim 9,
The pressure in the reactor of the ethylene monomer is 6 to 150 atm, the polymerization reaction temperature is 60 ℃ to 250 ℃ characterized in that the ethylene homopolymer or a copolymer of ethylene and α-olefin. The method of claim 5,
The weight average molecular weight of the copolymer is 80,000 to 500,000 and the molecular weight distribution (Mw / Mn) is an ethylene homopolymer or a method of producing a copolymer of ethylene and α-olefin, characterized in that 1.5 to 4.1. An ethylene homopolymer or a copolymer of ethylene and an -olefin prepared using the transition metal compound according to any one of claims 1 to 4 as a catalyst. Ethylene homopolymer or copolymer of ethylene and α-olefin prepared using the transition metal compound according to claim 5 as a catalyst composition.