JPH08319313A - Ethylene-based polymer - Google Patents

Abstract

PURPOSE: To obtain an ethylenic polymer having high melt flowability, excellent molding stability and mechanical properties. CONSTITUTION: This ethylene-based polymer is an ethylene homopolymer or copolymer and has (a) 3,000-1,000,000 weight-average molecular weight(Mw) measured by GPC method, (b) 850-970kg/m<2> . density, (c) 31-84kJ/mol activation energy (ΔEa) of melt flow and (d) the relation between the ratio Mw/Mn of the weight-average molecular weight(Mw) and the number-average molecular weight (Mn) measured by GPC method and the die swell ratio (DR) satisfying the formula DR>=0.09×(Mw/Mn)+1.20.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ethylene polymer, and more specifically, ethylene having high melt flowability, excellent molding stability (die swell ratio), and good mechanical properties (tensile impact strength, etc.). The present invention relates to a homopolymer or a copolymer.

[0002]

2. Description of the Related Art Conventionally, ethylene-based polymers such as polyethylene and ethylene-α-olefin copolymers have been widely used in many fields as general-purpose resins. However, this ethylene-based polymer has the following (1)-
There is a problem as shown in (3). That is,
(1) Linear low-density polyethylene (L-LDPE) and high-density polyethylene (HDPE) have a low activation energy (ΔEa) of melt flow and are low-density polyethylene (L-LDPE).
Since the resin fluidity is lower than that of DPE), the moldability is poor, and in particular, the moldability of the high molecular weight polymer is significantly poor. Similarly, the die swell ratio in the molten state is small and the molding stability is inferior to that of LDPE. (2) LDPE shows good molding characteristics, but mechanical properties are L-LDPE and HDPE.
Inferior to (3) In recent years, a homogeneous metallocene-based catalyst has been developed, which has excellent copolymerizability between olefins, has a narrow molecular weight distribution of the obtained polymer, and has extremely high catalytic activity as compared with conventional vanadium-based catalysts. It has become clear that On the other hand, however, the polymer obtained with this metallocene-based catalyst has a narrow molecular weight distribution, and therefore has many problems in molding processing characteristics, and restrictions are unavoidable in blow molding, inflation molding, cast molding and the like.

In order to solve such problems, various olefin polymers having long-chain branching have been disclosed. For example, (1) an α, ω-diene, an olefin-based copolymer having a long chain branch using a cyclic endomethylene-based diene (JP-A-47-34981), (2) a non-conjugated diene and an olefin When the copolymerization is carried out, the polymerization is carried out in two stages, and a method for producing a copolymer in which the content of non-conjugated diene in the high molecular weight portion is higher than that in the low molecular weight portion (JP-A-59-59).
56412), (3) ethylene / α-olefin / 1,5 using a metallocene / aluminoxane-based catalyst.
-Hexadiene copolymer (Japanese Patent Publication No. 1-501555), (4) Copolymerizing α, ω-dienes with ethylene using a zero-valent or divalent nickel compound and a specific aminobis (imino) compound as a catalyst. Therefore, a method of introducing a long chain branch (JP-A-2-261809), (5) a short chain branch and a long chain obtained by polymerizing only ethylene using the same catalyst component as the above (4) Polyethylene including both branches (Japanese Patent Laid-Open No. 3-277610) is disclosed. However, in the copolymer of (1) above, the diene component participates in the formation of long chain branching, and at the same time, a crosslinking reaction occurs simultaneously, gel is generated at the time of film formation, and conversely, the melting property deteriorates. The control range is extremely narrow, the copolymerization reactivity is low, and there are problems such as deterioration of physical properties due to formation of low molecular weight substances. In the method for producing a copolymer of (2), since the long-chain branch is introduced into the high-molecular weight component, the increase in the molecular weight due to cross-linking is remarkable, and insolubilization and gelation may occur at the same time. Due to its small size, the copolymerization reactivity is low, and there are problems such as deterioration of physical properties due to the formation of low molecular weight substances. Further, the copolymer (3) has a narrow molecular weight distribution and is disadvantageous for blow molding, film molding, etc., and also forms a branch point due to the progress of cyclization reaction of 1,5-hexadiene. There are drawbacks such as low effective monomer concentration. Furthermore, the method (4) of introducing long chain branching has problems such as gel generation and a narrow control range of physical properties. Further, the polyethylene (5) is a polymer containing no ethyl branch or butyl branch, and since physical properties such as density are controlled by the methyl branch, there is a problem that mechanical properties tend to deteriorate. are doing.

In addition, a method for producing an ethylene-based polymer imparted with a processing property by a copolymerization method, for example, a high-molecular weight polymer ([η] = 10 to 20 deciliter / g) is produced by prepolymerization, and then ethylene is produced by main polymerization. A method for producing a / α-olefin copolymer has been disclosed (Japanese Patent Laid-Open No. Hei 4 (1998) -19984).
-55410 publication). However, this method shows the effect of changing the melting characteristics of the obtained copolymer and increasing the melt tension, but has the drawback that film gel is likely to occur. Furthermore, an ethylene-based polymer using a metallocene-based catalyst and a method for producing the same, for example, (1) a method for producing an ethylene-based polymer using a constrained geometry type catalyst, and an ethylene-based copolymer obtained by the method (Japanese Patent Laid-Open No. HEI 3) -163088, WO93 / 0822
No. 1), (2) a method for producing a polyolefin by a supported metallocene catalyst using a porous inorganic oxide (aluminum compound) as a carrier (JP-A-4-100808), and (3) a specific hafnium-based catalyst. An ethylene / α-olefin copolymer having a narrow molecular weight distribution derived from ethylene and α-olefin and having improved melt flow characteristics (Japanese Patent Laid-Open No. 2-276807) is disclosed. However, in the above technique (1), the obtained ethylene-based copolymer has a narrow molecular weight distribution and a narrow compositional distribution, and both cannot be controlled individually. Furthermore, this ethylene-based copolymer contains
Although there is a statement that long-chain branching is present and it has excellent processing characteristics, that is, melt flow characteristics, it is still insufficient, and other important processing characteristics, especially molding stability (swell ratio, melt tension, etc.) There is no specific description. Further, in the production method of (2) above, the obtained ethylene and α-
Copolymers with olefins are said to have a large die swell ratio, but considering the relationship of the die swell ratio to the melting point of the ethylene / butene-1 copolymer disclosed herein,
It is clear that the die swell ratio decreases with increasing melting point. Therefore, it is not possible to provide a copolymer in which the die swell ratio related to neck-in, which is a problem when forming a film or a sheet, is controlled in a wide melting point range. On the other hand, what is disclosed in (3) is a copolymer containing an α-olefin unit as an essential unit, and does not include a copolymer having a resin density of more than 0.92 g / cm ³ . Further, as in (1), the molecular weight distribution and the composition distribution are narrow, and both of them cannot be controlled individually.

[0005]

Under these circumstances, the present invention provides ethylene having high melt fluidity, excellent molding stability (die swell ratio), and good mechanical properties (tensile impact strength, etc.). The purpose is to provide a polymer.

[0006]

Means for Solving the Problems As a result of intensive studies to develop an ethylene polymer having the above-mentioned properties, the present inventors have found that it is a homopolymer of ethylene or ethylene and other ethylenically unsaturated bonds. Which is a copolymer with at least one of the monomers having, the molecular weight, the density and the activation energy of melt flow in a specific range, and the molecular weight distribution and the die swell ratio have a specific relationship, It has been found that it can meet the purpose. The present invention has been completed based on such findings. That is, the present invention provides an ethylene homopolymer or a copolymer of ethylene and at least one other monomer having an ethylenically unsaturated bond, which is measured by (a) gel permeation chromatography method (GPC method). The weight average molecular weight (Mw) in terms of polyethylene is in the range of 3,000 to 1,000,000, and (b) the resin density (d) is 850 to 970 k.
g / m ³ range, (c) melt flow activation energy (ΔEa) in the range of 31 to 84 kJ / mol, and (d) polyethylene equivalent weight average molecular weight measured by GPC method ( Mw) and number average molecular weight (M
An ethylene polymer characterized in that the relationship between the ratio Mw / Mn with n) and the die swell (D _R ) satisfies the formula D _R ≧ 0.09 × (Mw / Mn) +1.20. It is a thing. The ethylene polymer of the present invention is a homopolymer of ethylene or a copolymer of ethylene and at least one other monomer having an ethylenically unsaturated bond. In the copolymer, the monomer having an ethylenically unsaturated bond used as a comonomer has 3 to 20 carbon atoms.
[Alpha] -olefins, styrenes, cyclic olefins and diolefins are preferred.

Examples of the α-olefin having 3 to 20 carbon atoms include propylene; 1-butene-; 1-pentene; 4-methyl-1-pentene; 1-hexene; 1-octene; 1-decene, 1-. Examples include dothecene; 1-tetradecene; 1-hexadecene; 1-octadecene; 1-eicosene. Examples of styrenes include styrene and α-methylstyrene, p-methylstyrene; o-methylstyrene; m-methylstyrene;
4-dimethylstyrene; 2,6-dimethylstyrene;
3,5-dimethylstyrene; alkylstyrene such as p-tert-butylstyrene, p-chlorostyrene; o
-Chlorostyrene; m-chlorostyrene; p-bromostyrene; o-bromostyrene; m-bromostyrene; p
-Fluorostyrene; o-fluorostyrene; m-fluorostyrene; halogenated styrene such as o-methyl-p-fluorostyrene; 4-vinylbiphenyl; 3-vinylbiphenyl; vinylphenyls such as 2-vinylbiphenyl; 1- (4-vinylphenyl) -naphthalene;
2- (4-vinylphenyl) -naphthalene; 1- (3-
Vinylphenyl) -naphthalene; 2- (3-vinylphenyl) -naphthalene; 1- (2-vinylphenyl) -naphthalene; vinylphenylnaphthalenes such as 2- (2-vinylphenyl) -naphthalene. The cyclic olefins having 3 to 20 carbon atoms are preferable, and specifically, cyclopentene; cyclohexene; norbornene; 1-methylnorbornene; 5-methylnorbornene; 7-methylnorbornene; 5,6-
Examples include dimethylnorbornene; 5,5,6-trimethylnorbornene; 5-ethylnorbornene; 5-propylnorbornene; 5-phenylnorbornene; 5-benzylnorbornene.

On the other hand, diolefins include compounds formed from at least two residues of the same or different type selected from α-olefin residues, styrene residues and cyclic olefin residues, and cyclic diene compounds. A polyfunctional monomer selected from the above is preferably used. Examples of such polyfunctional monomers include linear or branched acyclic diene compounds, monocyclic alicyclic diene compounds, polycyclic alicyclic diene compounds, cycloalkenyl-substituted alkenes, and aromatic rings. Examples of the diene compound include a diene compound having an α-olefin residue and a styrene residue in one molecule. Examples of the linear or branched acyclic diene compound include 1,4-pentadiene, 1,4-hexadiene,
1,5-hexadiene, 1,6-octadiene, 1,7
-Octadiene, 1,9-decadiene, 1,11-dodecadiene, 2-methyl-1,4-pentadiene, 2-methyl-1,5-hexadiene, 3-ethyl-1,7-octadiene, etc. Examples of the alicyclic diene compound include 1,3-cyclopentadiene and 1,4-
Cyclohexadiene, 1,5-cyclooctadiene,
1,5-cyclododecadiene, 1,2-divinylcyclohexane, 1,3-divinylcyclohexane and the like can be mentioned. Examples of the polycyclic alicyclic diene compound include dicyclopentadiene, norbornadiene, tetrahydroindene, methyltetrahydroindene, bicyclo- (2,2,1) -hepta-2,5-diene, 5-methyl-2, 5-norbornadiene, and further alkenyl,
Norbornenes of alkylidene, cycloalkenyl and cycloalkylidene, such as 5-methyl-2-norbornene, 5-ethylidene-2-norbornene, 5-
Examples include isopropylidene-2-norbornene, 5-vinylnorbornene, 5-butenylnorbornene, 5- (4-cyclopentenyl) -2-norbornene, 5-cyclohexylidene-2-norbornene and the like.

Further, the cycloalkenyl-substituted alkenes include, for example, allylcyclohexene, vinylcyclooctene, allylcyclodecene, vinylcyclododecene, and the diene compound having an aromatic ring includes, for example, p-divinylbenzene, Examples thereof include m-divinylbenzene, o-divinylbenzene, di- (p-vinylphenyl) methane, 1,3-bis (p-vinylphenyl) propane and 1,5-bis (p-biphenyl) pentane. On the other hand, examples of the diene compound having a styrene residue as an α-olefin residue in one molecule include p- (2-propenyl) styrene, m- (2-propenyl) styrene, p- (3-butenyl) styrene. , M-
(3-butenyl) styrene, o- (3-butenyl) styrene, p- (4-pentenyl) styrene, m- (4-pentenyl) styrene, o- (4-pentenyl) styrene, p- (7-octenyl). Styrene, p- (1-methyl-3-butenyl) styrene, p- (2-methyl-3-)
Butenyl) styrene, m- (2-methyl-3-butenyl) styrene, o- (2-methyl-3-butenyl) styrene, p- (3-methyl-3-butenyl) styrene, p
-(2-ethyl-4-pentenyl) styrene, p- (3
-Butenyl) -α-methylstyrene, m- (3-butenyl) -α-methylstyrene, o- (3-butenyl) -α
-Methylstyrene, 4-vinyl-4 '-(3-butenyl) biphenyl, 4-vinyl-3'-(3-butenyl)
Biphenyl, 4-vinyl-4 '-(4-pentenyl) biphenyl, 4-vinyl-2'-(4-pentenyl) biphenyl, 4-vinyl-4 '-(2-methyl-3-butenyl) biphenyl and the like can be mentioned. To be

One of these comonomers may be used,
You may use it in combination of 2 or more type. In the ethylene-based copolymer, the content of the comonomer unit is 0.01 to
The range of 45 mol% is preferable, and when the diolefin unit is contained, the content of the diolefin unit is
It is usually 1 mol% or less, preferably 0.8 mol% or less, more preferably 0.6 mol% or less, and particularly preferably 0.4 mol% or less. If the content of this diolefin unit exceeds 1 mol%, a problem of gelation due to crosslinking may occur.
The ethylene polymer of the present invention is required to have the following properties. First, (a) the weight average molecular weight (Mw) in terms of polyethylene measured by the gel permeation chromatography method (GPC method) is 3,000 to 1,
It must be in the range of 00000. This Mw
Is less than 3,000, the mechanical properties are not sufficiently expressed,
If it exceeds 1,000,000, the moldability will be deteriorated. From the viewpoint of mechanical properties and moldability, the preferable range of Mw is
5,000 to 80,000, more preferably 7,000
It is about 70,000. Further, (b) the resin density (d) needs to be in the range of 850 to 970 kg / m ³ . The resin density (d) can be arbitrarily controlled within the above range by increasing or decreasing the content of the comonomer unit. In addition, as for this density, a press sheet prepared at a temperature of 190 ° C. and quenched is JIS K-67.
According to 60, it is a value measured by a density gradient tube at 23 ° C.

Next, (c) the activation energy (ΔEa) of melt flow is 31 to 84 kJ / mol (7.5 to 20 kca).
1 / mole). This ΔEa
Is less than 31 kJ / mol, sufficient melt fluidity cannot be obtained. From the viewpoint of melt flowability, a preferable activation energy (ΔEa) of melt flow is 33 to 79 kJ / mol (8.0 to 1).
9 kcal / mole), especially 36 to 75 kJ
A range of / mol (8.5-18 kcal / mol) is preferred. The activation energy of this melt flow (ΔEa)
Is the temperature 150 ℃, 170 ℃, 190 ℃, 210 ℃, 2
Frequency dependence of dynamic viscoelasticity at 30 ° C (10 ^{-2 -1}
0 ² rad / sec) was measured and temperature as the reference temperature of 170 ° C. - with time superposition principle, G at each temperature ', G' value calculated by the Arrhenius equation from the shift factor and the absolute temperature of the reciprocal of the ' Is. Furthermore, (d)
Ratio Mw / M of polyethylene-converted weight average molecular weight (Mw) and number average molecular weight (Mn) measured by GPC method
It is necessary that the relationship between n and the die swell ratio (D _R ) satisfies the equation D _R ≧ 0.09 × (Mw / Mn) +1.20. The D _R is [0.09 × (M
If it is less than w / Mn) +1.20], sufficient swell cannot be obtained, and problems such as neck-in may occur during extrusion molding. From the viewpoint of molding stability, it is preferable that Mw / Mn and the die swell ratio (D _R ) satisfy the relation of formula 2.5 ≧ D _R ≧ 0.09 × (Mw / Mn) +1.26. It is preferable to satisfy the relationship of 2.0 ≧ D _R ≧ 0.09 × (Mw / Mn) +1.33.

Here, the die swell ratio (D _R ) was determined by using a capillary nozzle manufactured by Toyo Seiki Seisakusho, Ltd. [capillary nozzle (diameter (D ₀ ) = 1.0 mm, length (L) = 10.0].
mm, L / D ₀ = 10, inflow angle = 90 °]
2.0 mm / min (shear rate 24.3 sec ^-1 ), temperature 190
The diameter of the strand obtained by extruding under the condition of ° was determined by measuring with laser light at a position 1 cm from the exit of the capillary. Further, the Mw and Mn are
Equipment: Waters ALC / GPC 150C, column: TSK HM + GMH6 × 2, flow rate: 1.0 ml / min, solvent: 1,2,4-trichlorobenzene. Furthermore, the ethylene polymer of the present invention has a tensile impact strength (E _imp [kJ / m ² ]) and a die swell ratio (D _R ).
It is preferable that the relationship between and satisfies the expression logE _imp ≧ −1.2 × D _R +5.0. logE _imp is [-1.2 × D
_If it is less than _R + 5.0], mechanical properties are insufficient, and it is particularly preferable that the relationship between E _imp and D _R satisfies the expression logE _imp ≧ −1.2 × D _R +5.2 from the viewpoint of mechanical properties. Is. The tensile impact strength (E _imp ) is a value measured according to ASTM D-1822 by attaching a jig for tensile impact strength measurement to an Izod tester. Further, the ethylene polymer of the present invention has a ratio Mw of the weight average molecular weight (Mw) in terms of polyethylene and the number average molecular weight (Mn) measured by the GPC method.
It is preferable that / Mn is in the range of 1.5 to 4. This M
When w / Mn is less than 1.5, the molecular weight distribution is too narrow, which causes problems in molding processing characteristics, and when w / Mn exceeds 4, mechanical properties are insufficient. Mw / M in terms of molding characteristics and mechanical properties
The more preferable range of n is 1.6 to 3.5, and especially 1.6 to
The range of 3.3 is preferable.

The ethylene polymer of the present invention can be used as a mixture with another thermoplastic resin. Examples of other thermoplastic resins include polyolefin-based resins, polystyrene-based resins, condensation-type high-molecular polymers, and addition-polymerization high-molecular polymers. Specific examples of the polyolefin resin include high-density polyethylene; low-density polyethylene;
Poly-3-methylbutene-1; poly-4-methylpentene-1; butene-1 as a comonomer component; hexene-
1; Octene-1; 4-Methylpentene-1; 3-methylbutene-1, linear low-density polyethylene, ethylene-vinyl acetate copolymer, saponified ethylene-vinyl acetate copolymer, ethylene -Acrylic acid copolymers, ethylene-acrylic acid ester copolymers, ethylene-based ionomers, polypropylene and the like.
Specific examples of the polystyrene-based resin include general-purpose polystyrene, isotactic polystyrene, and high-impact polystyrene (rubber-modified). Specific examples of the condensation polymer include polyacetal resin, polycarbonate resin, polyamide resin such as nylon 6, nylon 6.6, polyester resin such as polyethylene terephthalate and polybutylene terephthalate, polyphenylene ether resin, polyimide resin, polysulfone resin. , Polyethersulfone resin, polyphenylene sulfide resin and the like. Examples of the addition polymerization type high molecular weight polymer include, for example, a polymer obtained from a polar vinyl monomer and a polymer obtained from a diene monomer, specifically, polymethyl methacrylate, polyacrylonitrile, acrylonitrile-butadiene copolymer, acrylonitrile. Examples thereof include a butadiene-styrene copolymer, a diene polymer in which a diene chain is hydrogenated, and a thermoplastic elastomer. When the ethylene polymer of the present invention is mixed with another thermoplastic resin, the ethylene polymer 1 of the present invention
It is desirable to mix the other thermoplastic resin in an amount of 2 to 500 parts by weight, preferably 3 to 300 parts by weight with respect to 00 parts by weight.

Next, the method for producing the ethylene-based polymer of the present invention is not particularly limited as long as it is a method capable of obtaining the ethylene-based polymer having the above-mentioned properties, and various methods can be used. In particular, as a polymerization catalyst,
A method of homopolymerizing ethylene or copolymerizing ethylene with another monomer having an ethylenically unsaturated bond, using a compound containing (A) a transition metal compound and (B) an aluminumoxy compound as essential components. Is advantageous. As the transition metal compound of the component (A), those represented by the general formula (I) CpML _X-1 ... (I) are preferably used.

In the above general formula (I), M represents a metal element of Groups 3 to 10 of the periodic table or lanthanoid series.
Cp represents a cyclic compound group having 5 to 30 carbon atoms and having cyclopentadienyl or a substituted cyclopentadienyl skeleton, which is coordinated to M by a π bond in a η ⁵ -bonding mode, and L is coordinated to M by a σ bond. Locating σ ligand. When there are a plurality of Ls, each L may be the same or different. Examples of the σ ligand include R ′, OR ′, SR ′, SO
Preferable examples include ₃ R ′, NR′R ″, NO ₂ , a halogen atom, a 1-pyrrolyl group, and a 1-pyrrolidinyl group. Here, R ′ and R ″ are each 1 to 1 carbon atoms.
20 hydrocarbon groups are shown, and in NR′R ″, R ′ and R ″ may be the same or different from each other. This σ
When there are a plurality of ligands, each ligand may be the same or different, but at least two of them are preferably the same. And two or three of the σ ligands are O
More preferably R'or NR'R ''. Further, from the viewpoint of copolymerizability, it is particularly preferable that two or three σ ligands have the same OR ′. Further, x represents the valence of M.

There is one group consisting of a cyclic compound having 5 to 30 carbon atoms and having a cyclopentadienyl or substituted cyclopentadienyl skeleton coordinated by a π bond in the above M and η ⁵ -bonding mode, Further, the substituents on the substituted cyclopentadienyl skeleton may bond with each other to form a new cyclic structure. That is, a group having an indenyl skeleton, a substituted indenyl skeleton, a fluorenyl skeleton, and a substituted fluorenyl skeleton is also included in the cyclic compound group. Further, in the above R ′ and R ″, the number of carbon atoms is 1-2.
Examples of the hydrocarbon group of 0 include an alkyl group, a cycloalkyl group, an aryl group and an aralkyl group. Examples of the alkyl group include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group,
Isobutyl group, sec-butyl group, t-butyl group, pentyl group, hexyl group, octyl group, decyl group, dodecyl group, etc., as the cycloalkyl group, for example, cyclopentyl group, cyclohexyl group, etc., as the aryl group Examples of the aralkyl group include a phenyl group and a tolyl group, and examples of the aralkyl group include a benzyl group and a phenethyl group. Specific examples of OR 'include methoxy group, ethoxy group, n-propoxy group, isopropoxy group, n-butoxy group, isobutoxy group, se.
Examples thereof include alkoxy groups such as c-butoxy group, t-butoxy group, pentoxy group, hexoxy group, octoxy group and cyclohexoxy group, and aryloxy groups such as phenoxy group. Further, as a specific example of SR ′,
Methylthio group, ethylthio group, cyclohexylthio group,
Examples thereof include a phenylthio group. And S
Specific examples of O ₃ R ′ include methanesulfonyl group, ethanesulfonyl group, n-propanesulfonyl group, isopropanesulfonyl group, n-butanesulfonyl group, sec-
Examples thereof include an alkylsulfonyl group such as butanesulfonyl group, t-butanesulfonyl group, and isobutanesulfonyl group, and an arylsulfonyl group such as benzenesulfonyl group. Furthermore, specific examples of NR'R "include dimethylamino group, diethylamino group, di (n-propyl) amino group, diisopropylamino group, di (n-).
Butyl) amino group, diisobutylamino group, di (sec
-Butyl) amino group, di (t-butyl) amino group, dipentylamino group, dihexylamino group, dioctylamino group, diphenylamino group, dibenzylamino group and the like. Further, examples of the halogen atom include chlorine, bromine and iodine.

Examples of the transition metal compound represented by the general formula (I) include cyclopentadienyl titanium trimethyl; cyclopentadienyl titanium triethyl; cyclopentadienyl titanium tri (n-propyl); cyclopentadiene. Cyclopentadienyl titanium tri (n-butyl); cyclopentadienyl titanium triisobutyl; cyclopentadienyl titanium tri (sec-butyl); cyclopentadienyl titanium tri (t-butyl); methyl 1,2-dimethylcyclopentadienyl titanium trimethyl; 1,2,4-trimethylcyclopentadienyl titanium trimethyl; 1,2,3,4-tetramethylcyclopentadienyl titanium trimethyl; Pentamethylcyclopen Pentamethylcyclopentadienyl titanium triethyl; Pentamethylcyclopentadienyl titanium tri (n-propyl); Pentamethylcyclopentadienyl titanium triisopropyl; Pentamethylcyclopentadienyl titanium tri (n-butyl) ); Pentamethylcyclopentadienyl titanium triisobutyl; pentamethylcyclopentadienyl titanium tri (sec-butyl); pentamethylcyclopentadienyl titanium tri (t-butyl); cyclopentadienyl titanium trimethoxide; cyclo Pentadienyl titanium triethoxide; Cyclopentadienyl titanium tri (n-propoxide); Cyclopentadienyl titanium triisopropoxide; Cyclopentadienyl titanium triphenoxide; Methylcyclopenta (N-butyl) cyclopentadienyl titanium trimethoxide; dimethyl cyclopentadienyl titanium trimethoxide; dimethyl cyclopentadienyl titanium triethoxide; dimethyl cyclopentadienyl titanium tri (n-) Propoxide); dimethylcyclopentadienyl titanium triisopropoxide; dimethyl cyclopentadienyl titanium triphenoxide; di (t-butyl) cyclopentadienyl titanium trimethoxide; di (t-butyl) cyclopentadienyl titanium Triethoxide; Di (t-butyl) cyclopentadienyl titanium tri (n-propoxide); Di (t-butyl) cyclopentadienyl titanium triisopropoxide; Di (t-butyl) cyclopentadienyl titanium Triphenoxide; bis ( Dimethylsilyl) cyclopentadienyl titanium trimethoxide; Bis (dimethylsilyl) cyclopentadienyl titanium triethoxide; Bis (dimethylsilyl) cyclopentadienyl titanium tri (n-propoxide);
Bis (dimethylsilyl) cyclopentadienyl titanium triisopropoxide; Bis (dimethylsilyl) cyclopentadienyl titanium triphenoxide; Trimethyl cyclopentadienyl titanium trimethoxide; Trimethyl cyclopentadienyl titanium triethoxide; Trimethyl cyclo Pentadienyl titanium tri (n-propoxide); trimethylcyclopentadienyl titanium triisopropoxide; trimethylcyclopentadienyl titanium triphenoxide; triethylcyclopentadienyl titanium trimethoxide; [bis (dimethylsilyl), methyl ] Cyclopentadienyl titanium trimethoxide; [Di (t-butyl, methyl)] cyclopentadienyl titanium triethoxide; Tetramethylcyclopentadienyl titanium trimethoxide; Tramethylcyclopentadienyl titanium triethoxide; Tetramethylcyclopentadienyl titanium tri (n-propoxide); Tetramethylcyclopentadienyl titanium triisopropoxide; Tetramethylcyclopentadienyl titanium tri (n-butoxide) ); Tetramethylcyclopentadienyl titanium triisobutoxide; Tetramethyl cyclopentadienyl titanium tri (sec-butoxide); Tetramethyl cyclopentadienyl titanium tri (t-butoxide); Tetramethyl cyclopentadienyl titanium triphenoxide [Tetramethyl, 4-methoxyphenyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl,
4-Methoxyphenyl] cyclopentadienyl titanium triethoxide; [Tetramethyl, 4-methoxyphenyl] cyclopentadienyl titanium tri (n-propoxide); [Tetramethyl, 4-methoxyphenyl] cyclopentadienyl titanium Triisopropoxide; [Tetramethyl, 4-methoxyphenyl] cyclopentadienyl titanium triphenoxide; [Tetramethyl, 4-methylphenyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl, 4-methylphenyl] cyclo Pentadienyl titanium triethoxide; [tetramethyl, 4
-Methylphenyl] cyclopentadienyl titanium tri (n-propoxide); [Tetramethyl, 4-methylphenyl] cyclopentadienyl titanium triisopropoxide; [Tetramethyl, 4-methylphenyl] cyclopentadienyl titanium Triphenoxide; [Tetramethyl, benzyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl, benzyl] cyclopentadienyl titanium triethoxide; [Tetramethyl, benzyl]
Cyclopentadienyl titanium tri (n-propoxide); [Tetramethyl, benzyl] cyclopentadienyl titanium triisopropoxide; [Tetramethyl, benzyl] cyclopentadienyl titanium triphenoxide;
[Tetramethyl, 2-methoxyphenyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl, 2-
Methoxyphenyl] cyclopentadienyl titanium triethoxide; [Tetramethyl, 2-methoxyphenyl] cyclopentadienyl titanium triphenoxide; [Tetramethyl, ethyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl, ethyl] Cyclopentadienyl titanium triethoxide; [tetramethyl, ethyl] cyclopentadienyl titanium tri (n-propoxide);
[Tetramethyl, ethyl] cyclopentadienyl titanium triisopropoxide; [Tetramethyl, ethyl] cyclopentadienyl titanium triphenoxide; [Tetramethyl, n-butyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl , N-Butyl] cyclopentadienyl titanium triethoxide; [tetramethyl, n-
[Butyl] cyclopentadienyl titanium tri (n-propoxide); [Tetramethyl, n-butyl] cyclopentadienyl titanium triisopropoxide; [Tetramethyl, n-butyl] cyclopentadienyl titanium triphenoxide; Tetramethyl, phenyl] cyclopentadienyl titanium trimethoxide; [Tetramethyl, phenyl] cyclopentadienyl titanium triethoxide; [Tetramethyl, phenyl] cyclopentadienyl titanium triphenoxide; [Tetramethyl, dimethylsilyl] Cyclopentadienyl titanium trimethoxide; [Tetramethyl, dimethylsilyl] cyclopentadienyl titanium triphenoxide; Pentamethylcyclopentadienyl titanium trimethoxide; Pentamethylcyclopentadienyl titanium triethoxide Pentamethylcyclopentadienyl titanium tri (n-propoxide); pentamethylcyclopentadienyl titanium triisopropoxide; pentamethylcyclopentadienyl titanium tri (n-butoxide); pentamethylcyclopentadienyl titanium Triisobutoxide; pentamethylcyclopentadienyl titanium tri (sec-butoxide); pentamethylcyclopentadienyl titanium tri (t-butoxide); pentamethylcyclopentadienyl titanium tri (cyclohexoxide); pentamethylcyclopenta Dienyl titanium triphenoxide; cyclopentadienyl titanium tribenzyl; indenyl titanium trimethoxide; indenyl titanium triethoxide; indenyl titanium trimethyl; indenyl titanium tribenzyl; cyclopentadi Nyltitanium tri (methanesulfonyl); Trimethylcyclopentadienyl titanium (tribenzenesulfonyl); Tetramethylcyclopentadienyl titanium tri (ethanesulfonyl); Pentamethylcyclopentadienyl titanium tri (methanesulfonyl); Cyclopentadienyl titanium tris (Dimethylamine); trimethylcyclopentadienyl titanium tris (dimethylamine); pentamethylcyclopentadienyl titanium tris (dibenzylamine); cyclopentadienyl titanium tri (nitro); pentamethylcyclopentadienyl titanium tri ( Nitro)
Etc., and titanium in these compounds as zirconium, hafnium, chromium, etc.
Examples thereof include compounds substituted with a metal element of Group 10 to 10 or a lanthanoid series.

Further, cyclopentadienyl titanium dimethyl monochloride; cyclopentadienyl titanium monoethyl dichloride; cyclopentadienyl titanium di (n
-Propyl) monochloride; cyclopentadienyl titanium diisopropyl monochloride; cyclopentadienyl titanium di (n-butyl) monochloride; cyclopentadienyl titanium diisobutyl monochloride; cyclopentadienyl titanium di (sec-butyl) mono Chloride; cyclopentadienyl titanium di (t-butyl) monochloride; 1,2-dimethylcyclopentadienyl titanium dimethyl monochloride; 1,2,4-trimethylcyclopentadienyl titanium dimethyl monochloride; Three
4-Tetramethylcyclopentadienyl titanium dimethyl monochloride; pentamethyl cyclopentadienyl titanium dimethyl monochloride; cyclopentadienyl titanium monochlorodimethoxide; cyclopentadienyl titanium dichloromonoethoxide; cyclopentadienyl titanium monochloride (N-propoxide); cyclopentadienyl titanium monochlorodiisopropoxide; cyclopentadienyl titanium monochlorodiphenoxide; dimethylcyclopentadienyl titanium monochlorodimethoxide;
Dimethylcyclopentadienyl titanium monochlorodiethoxide; Dimethylcyclopentadienyl titanium monochlorodioxide (n-propoxide); Dimethylcyclopentadienyl titanium monochlorodiisopropoxide; Dimethylcyclopentadienyl titanium monochlorodiphenoxide;
Di (t-butyl) cyclopentadienyl titanium monochlorodimethoxide; bis (dimethylsilyl) cyclopentadienyl titanium monochlorodimethoxide; trimethylcyclopentadienyl titanium monochlorodimethoxide; trimethylcyclopentadienyl titanium monochlorodiphenoxide; triethyl Cyclopentadienyl titanium monochlorodimethoxide; [bis (dimethylsilyl), methyl] cyclopentadienyl titanium monochlorodimethoxide; tetramethylcyclopentadienyl titanium monochlorodimethoxide; tetramethylcyclopentadienyl titanium monochlorodimethoxide (n- Butoxide); tetramethylcyclopentadienyltitanium monochlorodiisobutoxide; tetramethylcyclopentadienyltitanium monochlorodoxy (sec-butoxide) Sid); tetramethylcyclopentadienyl titanium monochlorodisilane (t-butoxide);
[Tetramethyl, 4-methoxyphenyl] cyclopentadienyl titanium monochlorodimethoxide; [Tetramethyl, 4-methylphenyl] cyclopentadienyl titanium monochlorodimethoxide; [Tetramethyl, benzyl]
Cyclopentadienyl titanium monochlorodimethoxide;
[Tetramethyl, benzyl] cyclopentadienyl titanium monochlorodiphenoxide; [Tetramethyl, 2-methoxyphenyl] cyclopentadienyl titanium monochlorodimethoxide; [Tetramethyl, ethyl] cyclopentadienyl titanium monochlorodimethoxide; [Tetra [Methyl, ethyl] cyclopentadienyl titanium monochlorodiethoxide; [tetramethyl, n-butyl] cyclopentadienyl titanium monochlorodiethoxide; [tetramethyl, n-butyl] cyclopentadienyl titanium monochlorodieth (n- Propoxide); [Tetramethyl, n-
Butyl] cyclopentadienyl titanium monochlorodiisopropoxide; [tetramethyl, phenyl] cyclopentadienyl titanium monochlorodimethoxide; [tetramethyl, dimethylsilyl] cyclopentadienyl titanium monochlorodimethoxide; pentamethylcyclopentadienyl Titanium monochlorodimethoxide; pentamethylcyclopentadienyl titanium monochlorodiethoxide; pentamethylcyclopentadienyl titanium monochlorodioxide (cyclohexoxide); pentamethylcyclopentadienyl titanium monochlorodiphenoxide; indenyl titanium monochlorodimethoxide; Cyclopentadienyl titanium monochloro (methanesulfonyl); pentamethylcyclopentadienyl titanium monochlorobis (diethylamine); pentamethyi Substitution of cyclopentadienyl titanium monochlorobis [di (n-butyl) amine] and the like, and titanium in these compounds with zirconium, hafnium, chromium and the like, and further with metal elements of Groups 8 to 10 of the periodic table and lanthanoid series The compound which did is mentioned.

In the polymerization catalyst of the present invention, the transition metal compound as the component (A) may be used alone or in combination of two or more kinds. In the polymerization catalyst of the present invention, the aluminum oxy compound used as the component (B) has the general formula (II)

[0020]

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A chain aluminoxane represented by the general formula (III)

[0022]

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The cyclic aluminoxane represented by: can be preferably mentioned. In the general formulas (II) and (III), R ¹ represents a hydrocarbon group having 1 to 20 carbon atoms, preferably 1 to 12 carbon atoms such as an alkyl group, an alkenyl group, an aryl group and an arylalkyl group, and n and p Are each 3
It shows the integer of -50, preferably 7-40. Moreover, a plurality of R ^{1 s} present in the molecule may be the same or different. Examples of the method for producing the aluminoxane include a method in which an alkylaluminum and a condensing agent such as water are brought into contact with each other, but the means therefor is not particularly limited, and the reaction may be performed according to a known method. For example, a method of dissolving an organoaluminum compound in an organic solvent and bringing it into contact with water, water of crystallization contained in a metal salt,
There are a method of reacting adsorbed water of an inorganic substance or an organic substance with an organoaluminum compound, a method of reacting a tetraalkyldialuminoxane with a trialkylaluminum, and further reacting with water. The aluminum oxy compound as the component (B) may be used alone or in combination of two or more kinds. The polymerization catalyst in the present invention may optionally contain an organoaluminum compound as the component (C) in addition to the components (A) and (B). Here, the organoaluminum compound as the component (C) is represented by the general formula (IV) R ² _r AlQ _3-r (IV) [wherein, R ² is an alkyl group having 1 to 10 carbon atoms, and Q is Hydrogen atom, C1-C20 alkoxy group, C6-C20
Represents an aryl group or a halogen atom, and r is an integer of 1 to 3. ] The compound represented by these is used.

Specific examples of the compound represented by the general formula (IV) include trimethyl aluminum, triethyl aluminum, triisopropyl aluminum, triisobutyl aluminum, dimethyl aluminum chloride, diethyl aluminum chloride, methyl aluminum dichloride, ethyl aluminum dichloride, dimethyl. Aluminum fluoride, diisobutyl aluminum hydride, diethyl aluminum hydride, ethyl aluminum sesquichloride and the like can be mentioned. Of these, trimethylaluminum, triethylaluminum and tributylaluminum are particularly preferable from the viewpoint of catalytic activity and availability. The organoaluminum compound as the component (C) may be used alone or in combination of two or more.

Regarding the use ratio of the above-mentioned (A) catalyst component and (B) catalyst component in the polymerization catalyst used in the present invention, when the metal atom of the (A) component is titanium,
It is advantageous to select the molar ratio of component (B) / component (A) to be in the range of 2-1,000, preferably 5-200. When the metal atom of the component (A) is other than titanium, such as zirconium or hafnium, (B)
It is advantageous to select the component / (A) component molar ratio in the range of 10 to 1,000, preferably 20 to 500. Further, when the catalyst component (C) is used,
It is desirable to use the component (C) so that the molar ratio of the component (C) / the component (A) is in the range of 0.01 to 100, preferably 0.1 to 50. By using this (C) catalyst component, the polymerization activity per transition metal can be improved, but if it is too much, the organoaluminum compound is wasted and a large amount remains in the polymer, which is not preferable.
In the method of the present invention, at least one of the catalyst components can be used by supporting it on, for example, a solid inorganic carrier or organic carrier insoluble in a hydrocarbon solvent. Examples of the inorganic carrier include SiO ₂ , Al ₂ O ₃ , MgO and Zr.
O ₂ , TiO ₂ , Fe ₂ O ₃ , B ₂ O ₃ , CaO, Zn
O, BaO, ThO ₂ and mixtures thereof such as silica alumina, zeolite, ferrite, sepiolite,
Glass fiber, MgCl ₂ and Mg (O
Examples thereof include magnesium compounds such as C ₂ H ₅ ) ₂ .

On the other hand, examples of the organic carrier include polymers such as polystyrene, styrene-divinylbenzene copolymer, polyethylene, polypropylene, substituted polystyrene and polyarylate, starch and carbon. In addition, in the gas phase polymerization method and the like, the carrier is not particularly limited to a carrier insoluble in a hydrocarbon solvent. Among these carriers, especially MgCl ₂ , Mg (OC ₂ H ₅ ) ₂ , Si
O ₂ , Al ₂ O _{3 and the} like are preferable. The average particle size of the carrier is 1 to 300 μm, preferably 10 to 200 μm,
More preferably, the range of 20 to 100 μm is desirable. Regarding the polymerization conditions, the polymerization temperature is preferably as high as possible without impairing the catalytic activity, and is usually -100 to 300 ° C, preferably -50 to 200 ° C, more preferably 10 to 18 ° C.
It is selected in the range of 0 ° C. The polymerization pressure is normal pressure to 150 k.
g / cm ² G, preferably atmospheric pressure to 100 kg / cm ² G
The range is good.

The polymerization method is not particularly limited and may be slurry polymerization method, gas phase polymerization method, bulk polymerization method, solution polymerization method,
Any method such as suspension polymerization method may be used. When a polymerization solvent is used, for example, aromatic hydrocarbons such as benzene, toluene, xylene and ethylbenzene, alicyclic hydrocarbons such as cyclopentane, cyclohexane and methylcyclohexane, aliphatic hydrocarbons such as pentane, hexane, heptane and octane. , Halogenated hydrocarbons such as chloroform and dichloromethane can be used. These solvents may be used alone or in combination of two or more. Further, a monomer such as α-olefin may be used as a solvent. Depending on the polymerization method, it can be carried out without a solvent.

When ethylene is copolymerized with another monomer, the charging ratio of each monomer is appropriately selected according to the desired resin density. Further, as a method for controlling the molecular weight of the polymer, the amount of chain transfer agent such as hydrogen used,
Examples include the type of each catalyst component, the amount used, the polymerization temperature, and the selection of ethylene pressure. For example, the use ratio of the monomer and the polymerization catalyst is selected so that the molar ratio of the monomer / (A) catalyst component is usually 10 to 1 × 10 ⁷ , and preferably 100 to 1 × 10 ⁶ .

[0029]

EXAMPLES Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples. The physical properties of the ethylene polymer were measured according to the methods described in the text of the specification. Example 1 (1) Preparation of methylaluminoxane 200 ml of Albemarle's methylaluminoxane (toluene solution) was placed in a glass container with an internal volume of 500 ml which had been replaced with nitrogen, and nitrogen was added to water in a glass container with an internal volume of 100 ml. The stirring was continued for 80 hours while circulating a nitrogen gas containing a trace amount of water obtained by circulating the gas. The amount of water required for the reaction calculated from the weight reduction of water was 24 mol% based on the aluminum atom of methylalnoxane. (2) Production of ethylene / octene-1 copolymer In a pressure-resistant stainless steel autoclave having an internal volume of 1 liter, 390 ml of dehydrated toluene, 10 ml of dehydrated octene-1 and methylaluminoxane 1 prepared in the above (1) were introduced under a nitrogen stream. Then, mmol (in terms of aluminum atom) was added and the temperature was raised to 60 ° C. in a stirring state.
After holding for 5 minutes in this state, pentamethylcyclopentadienyl titanium trimethoxide [Cp ^* Ti
(OMe) ₃ ] 10 μmol was added and the temperature was raised to 65 ° C. After that, add hydrogen to 0.5 kg / cm ² G with a pressure gauge.
Then, ethylene was continuously introduced with a pressure gauge at a constant pressure of 4 kg / cm ² G for 60 minutes. After the completion of the polymerization reaction, the pressure was released, the polymer was reprecipitated in methanol and collected by filtration. Then, it was dried under reduced pressure to obtain 37.8 g of a polymer.

(3) Evaluation of ethylene / octene-1 copolymer The ethylene / octene-1 copolymer obtained in (2) above has a resin density (d) of 909 kg / m ³ and GPC.
Polyethylene-equivalent weight average molecular weight (Mw) is 85,000 and number average molecular weight (Mn) is 35.9
00, the molecular weight distribution Mw / Mn was 2.37. Also,
Melt flow activation energy (ΔEa) is 40.2kJ /
Mol (9.6kcal / mol), die swell ratio (D _R)
Is 1.72 and tensile impact strength (E _imp ) is 1410 kJ / m
^{Was 2} .

Example 2 A copolymer was prepared in the same manner as in Example 1, except that 0.2 mmol of 5-vinylnorbornene was added after the addition of dehydrated octene-1. After drying under reduced pressure, 28.4 g of a polymer was obtained. Table 1 shows the evaluation results of the physical properties of this copolymer. Comparative Example 1 In Example 1, methyl aluminoxane (toluene solution) manufactured by Albemarle was used for the polymerization as it was, and the ethylene partial pressure during the polymerization reaction was 8 kg / cm ² G and the reaction time was 12
A copolymer was produced in the same manner as in Example 1 except that the time was 0 minutes. After drying under reduced pressure, 18.4 g of a polymer was obtained. Table 1 shows the evaluation results of the physical properties of this copolymer. Comparative Example 2 300 ml of dehydrated toluene, 100 ml of dehydrated octene-1 and Example 1-in a pressure-resistant stainless steel autoclave having an internal volume of 1 liter under a nitrogen stream.
2 mmol of methylaluminoxane prepared in (1) (in terms of aluminum atom) was added, and the temperature was raised to 60 ° C. with stirring. After maintaining this state for 5 minutes, dicyclopentadienyl zirconium dichloride (Cp ₂ ZrCl _2
2 ) 1.0 micromol was added and the temperature was raised to 80 ° C.
Then, ethylene was continuously introduced with a pressure gauge at a constant pressure of 8 kg / cm ² G for 30 minutes. After the completion of the polymerization reaction, the pressure was released, the polymer was reprecipitated in methanol and collected by filtration. After drying under reduced pressure, 42.5 g of a polymer was obtained. Table 1 shows the evaluation results of the physical properties of this copolymer.

[0032]

[Table 1]

[0033]

[Table 2]

[0034]

The ethylene-based polymer of the present invention is a homopolymer or copolymer of ethylene, has high melt fluidity and excellent molding stability (die swell ratio).
It has good mechanical properties (tensile impact strength, etc.) and is suitable for use in the fields of blow molding and cast molding, where molding processing was difficult with conventional L-LDPE. Further, since a blend such as LDPE is unnecessary, a molded product having high physical properties can be obtained, and the process can be simplified, which is advantageous in terms of cost.

Claims (4)

[Claims] 1. A homopolymer of ethylene or a copolymer of ethylene and at least one other monomer having an ethylenically unsaturated bond, which is measured by (a) gel permeation chromatography method (GPC method). Polyethylene-equivalent weight average molecular weight (Mw) is 3,000-
In the range of 1,000,000, (b) the resin density (d) is in the range of 850 to 970 kg / m ³ ,
(C) Activation energy (ΔEa) of melt flow is 31 to
In the range of 84 kJ / mol, and (d) the ratio Mw / Mn of polyethylene-equivalent weight average molecular weight (Mw) and number average molecular weight (Mn) measured by GPC method,
An ethylene polymer characterized in that the relationship with the die swell ratio (D _R ) satisfies the expression D _R ≧ 0.09 × (Mw / Mn) +1.20. 2. Tensile impact strength (E _imp [kJ / m ² ])
The ethylene-based polymer according to claim 1, wherein the relationship between the swell ratio (D _R ) and the die swell ratio satisfies the formula logE _imp ≧ −1.2 × D _R +5.0. 3. A monomer having an ethylenically unsaturated bond is an α-olefin having 3 to 20 carbon atoms, a styrene,
The ethylene polymer according to claim 1, which is at least one selected from cyclic olefins and diolefins. 4. The ratio Mw / Mn of the weight average molecular weight (Mw) in terms of polyethylene and the number average molecular weight (Mn) measured by gel permeation chromatography (GPC method) is in the range of 1.5 to 4. The ethylene-based polymer according to claim 1.