JP2013122013A - Method for producing olefin polymerization catalyst - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a dual catalyst favorable in catalytic properties such as bulk density and flowability and capable of producing a propylenic polymer including a long chain branch using a catalyst component producing a macromer and another catalyst component copolymerizing the same.SOLUTION: In the method for producing an olefin polymerization catalyst at least including the following components [A-1], [A-2], [B] and [C], the processes [I] to [III] are sequentially performed as follows: process [I] of bringing the components [A-1], [B] and [C] into contact with each other to produce a contact product (1); process [II] of cleansing the contact product (1) using an inactive hydrocarbon solvent so that a cleansing rate becomes ≤1/10 to generate a cleansed material; and process [III] of producing a contact product (2) by bringing the cleansed material into contact with the component [A-2] {wherein [A-1] is a compound (with a bisindenyl structure) represented by general formula (a1) or the like; [A-2] is a compound (e.g. with a biscyclopentadienyl structure) represented by general formula (a2); [B] is an ion-exchangeable layered silicate [B-4] or the like; and [C] is an organic aluminum compound}.

Description

  The present invention relates to a method for producing an olefin polymerization catalyst used in the polymerization of, for example, a propylene-based polymer, and more specifically, a long chain using a catalyst component that forms a macromer and a catalyst component that copolymerizes the catalyst component. The present invention relates to a method for producing a highly active two-way catalyst capable of producing a propylene-based polymer containing a branch.

Conventionally, polypropylene has high mechanical strength such as rigidity, excellent balance of physical properties, chemically stable, excellent weather resistance, hardly affected by chemicals, etc., and has a high melting point, excellent heat resistance, and light weight. Since it has features such as being inexpensive, it is widely used in many fields. However, ordinary polypropylene has low melt tension and melt viscoelasticity, and has problems such as restrictions on use in thermoforming, foam molding, blow molding and the like.
In order to solve these problems, a method has been proposed in which melt tension can be increased by introducing crosslinking or long chain branching of polypropylene itself, and various attempts have been made.
As such a method, a macromer copolymerization method mainly utilizing a metallocene catalyst has been recently proposed.

A metallocene catalyst is a transition metal compound having at least one conjugated five-membered ring ligand in a broad sense, and a ligand having a crosslinked structure is generally used for propylene polymerization. Initially, ethylenebis (indenyl) zirconium dichloride and ethylenebis (4,5,6,7-tetrahydroindenyl) zirconium dichloride found as complexes capable of producing isotactic polyolefin (see, for example, Patent Document 1). Dimethylsilylene bis-substituted cyclopentadienyl zirconium dichloride having a silylene group as a bridging group (for example, see Patent Document 2), dimethylsilylene bis (indenyl) zirconium dichloride (for example, see Patent Document 3), cyclopentadienyl. Dimethylsilylenebis (2-methylindenyl) zirconium dichloride whose stereoregularity and molecular weight have been improved to some extent by attaching a substituent next to the crosslinking group (2-position) of the compound (see, for example, Patent Document 4), Ally in 4th position Dimethylsilylene bis (2-methyl-4-phenylindenyl) zirconium dichloride (see, for example, Patent Document 5) and dimethylsilylene bis (2-methyl-), which are further improved in activity, stereoregularity and molecular weight by introducing a group 4-phenyl-4-hydroazurenyl) zirconium dichloride (see, for example, Patent Document 6), and more recently, dichloro (1,1′-dimethylsilylene) in which a specific substituent is introduced at a specific position of the 4-position aryl group Bis (2-ethyl-4- (3-chloro-4-t-butylphenyl) -4H-azurenyl)) hafnium (see, for example, Patent Document 7), which has a bulky hetero substituent introduced at the 2-position (For example, refer to Patent Documents 8 to 11.) and the like.
These are mainly for the purpose of improving the catalytic activity and the melting point and molecular weight of the resulting polypropylene, and there is no suggestion of the suitability for producing macromers or polypropylene having long chain branches.

On the other hand, as a macromer copolymerization method using a metallocene catalyst, for example, a propylene macromer having a vinyl structure at the terminal can be obtained in a first stage of polymerization (hereinafter also referred to as a macromer synthesis step) depending on a specific catalyst and specific polymerization conditions. And then copolymerizing with propylene under a specific catalyst and specific polymerization conditions in the second stage of polymerization (hereinafter also referred to as a macromer copolymerization step), so that there is no higher order crosslinking and as polypropylene. Has been proposed (hereinafter also referred to as a macromer copolymerization method) in which the original chemical stability is not impaired, the recyclability is excellent, and there is no concern about the formation of a gel for improving the melt tension. (See Patent Documents 12 and 13.)
Further, a homopolymerization method has been proposed in which a macromer synthesis step and a macromer copolymerization step are simultaneously performed using a single complex with respect to the above-described multistage polymerization method (see, for example, Patent Document 14).
However, with this known technique, the amount of macromer produced and the amount of macromer copolymerization are not necessarily sufficient, and the effect of improving the melt properties was insufficient.

In view of the situation as described above, the present inventors supported a long chain by supporting two types of complexes of a macromer production complex having a specific structure and a macromer copolymer complex having a specific structure on the same carrier. The present inventors have found a method for producing a propylene polymer having improved melt properties into which branching has been introduced (see Patent Documents 15 to 18).
Therefore, in producing such a propylene polymer having improved melt properties, it is desired to produce such a polymer industrially and economically efficiently, and a polymerization catalyst therefor, It is strongly desired to find a method for producing the polymerization catalyst.
As a method for obtaining such a highly active catalyst, a method focusing on the order in which two kinds of complexes are brought into contact with the support, and after conducting preliminary polymerization by bringing one kind of complex into contact with the support first, another kind of catalyst is obtained. A method of bringing a complex of the above and a carrier into contact with each other has been found (see Patent Documents 19 and 20).
However, the catalyst obtained by such a production method still has room for improvement in handling.
That is, as disclosed above, two types of complexes of a macromer production complex having a specific structure and a macromer copolymer complex having a specific structure are used, and prepolymerization is carried out on the same carrier. In particular, when the prepolymerization is performed by low-pressure slurry polymerization, the molecular weight produced by the macromer production complex is small, so that the prepolymerized polymer is eluted in the solvent, and the prepolymerization ratio does not increase. Problems arise. As described above, if there are many elution components and the prepolymerization ratio is not increased, the properties such as the decrease in bulk density and the flowability of the prepolymerized catalyst are deteriorated, and there is a problem that inconvenience occurs in the handling of the catalyst.

JP-A 61-130314 JP-A-1-301704 JP-A-1-275609 JP-A-4-268307 Japanese Patent Application Laid-Open No. 6-100579 Japanese Patent Laid-Open No. 10-226712 JP 2003-292518 A JP 2002-194016 A Special Table 2002-535339 JP 2004-2259 A JP 2004-352707 A JP-T-2001-525460 JP 10-338717 A Special table 2002-523575 gazette JP 2009-108247 A JP 2009-057542 A JP 2009-040959 A JP 2009-40959 A JP 2010-196036 A JP 2010-196037 A

  In view of the above-mentioned problems of the prior art, an object of the present invention is to produce a propylene-based polymer containing a long chain branch by using a catalyst component that generates a macromer and a catalyst component that copolymerizes the macromer. An object of the present invention is to provide a method for producing a two-way catalyst having good catalytic properties such as density and flowability.

  In order to solve the above-mentioned problems, the present inventors have made extensive studies and, as a result, in a method for producing a two-way catalyst using two specific metallocene catalyst components, contact with the optimum organoaluminum in each complex As a condition, first contact the complex, organoaluminum and support, then wash with an inert hydrocarbon solvent, then contact the second complex, organoaluminum and support, It has been found that when propylene is polymerized, it becomes a highly active catalyst, and the present invention has been completed.

According to a first aspect of the present invention, there is provided a process for producing an olefin polymerization catalyst comprising at least the following components [A-1], [A-2], [B] and [C], comprising the following step [I ]-[III] are performed sequentially, The manufacturing method of the catalyst for olefin polymerization characterized by the above-mentioned is provided.
Step [I]: A step of producing a contact product (1) by bringing component [A-1] into contact with components [B] and [C].
Step [II]: a step of washing the contact product (1) obtained in step [I] with an inert hydrocarbon solvent so that the washing rate is 1/10 or less to produce a washed product. .
However, the cleaning rate is determined by the following calculation formula.
W ₁ = (V ₀ + P ₁ −d ₁ ) / (V ₀ + P ₁ )
W ₂ = (V ₁ + P ₂ −d ₂ ) / (V ₁ + P ₂ )
_{W n = (V n-1} + P n -d n) / (V n-1 + P n)
Cleaning rate = W ₁ × W ₂ .. × W _n
In the calculation formula, the symbols have the following meanings.
W _n : Cleaning rate of the nth time (0 time indicates before cleaning, and W ₀ = 1)
V _n-1 : (n-1) Solution amount after the n-th washing d _n : Amount of solution extracted at the n-th washing P _n : Additional inert hydrocarbon solvent amount at the n-th washing step [III]: Step A step of producing a contact product (2) by bringing the component [A-2] into contact with the washed product obtained in [II].
However, the molar ratio [A-1] / [A-2] of [A-1] to component [A-2] is 1.0 to 99.0.
Component [A-1]: A metallocene compound that forms a polymerization catalyst for producing an olefin macromer. However, a metallocene compound that forms a polymerization catalyst for generating an olefin macromer generates a propylene homopolymer having a terminal vinyl ratio (Rv) of 0.5 or more when propylene homopolymerization is performed at 70 ° C. It is a metallocene compound that forms a polymerization catalyst.
Here, the terminal vinyl ratio (Rv) is defined by the following formula.
Rv = Mn / 21000 × [Vi]
(In the formula, Mn is the number average molecular weight determined by GPC, and [Vi] is the number of terminal vinyl groups per 1000 C calculated from ¹³ C-NMR.)
Component [A-2]: Compound represented by the general formula (a2).

[In General Formula (a2), E ²¹ and E ²² are each independently a cyclopentadienyl group, an indenyl group, a fluorenyl group, or an azulenyl group, and each may have a substituent (provided that The substituent is not a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur.) Q ²¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or a germylene group optionally having a hydrocarbon group having 1 to 20 carbon atoms, and M ²¹ represents zirconium or hafnium. , X ²¹ and Y ²¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogen having 1 to 20 carbon atoms. Represents a hydrocarbyl group, an amino group, or an alkylamino group having 1 to 20 carbon atoms. ]
Component [B]: an ionic compound or Lewis acid [B-] capable of reacting with the aluminum oxy compound [B-1], the transition metal compounds [A-1] and [A-2] to be converted into a cation. 2], at least one selected from the group consisting of solid acid fine particles [B-3] and ion-exchange layered silicate [B-4].
Component [C]: an organoaluminum compound.

  According to the second invention of the present invention, in the first invention, the component [A-1] is a compound represented by the general formula (a1). Is provided.

[In General Formula (a1), R ¹¹ and R ¹² each independently represent a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur. R ¹³ and R ¹⁴ each independently represent halogen, silicon, oxygen, sulfur, nitrogen, boron, phosphorus, or a C 6-16 aryl that may contain a plurality of hetero elements selected from these Or a heterocyclic group having 6 to 16 carbon atoms containing nitrogen, oxygen or sulfur. Further, M ¹¹ represents zirconium or hafnium, and X ¹¹ and Y ¹¹ each independently represent a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, or a hydrocarbon group having 1 to 20 carbon atoms. A silyl group, a halogenated hydrocarbon group having 1 to 20 carbon atoms, an amino group or an alkylamino group having 1 to 20 carbon atoms, Q ¹¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms, carbon number It represents a silylene group or a germylene group which may have 1 to 20 hydrocarbon groups. ]

  According to a third aspect of the present invention, in the first aspect, the component [A-1] is a compound represented by the general formula (a3). Is provided.

[In General Formula (a14), R ^{141 to} R ¹⁴⁴ are each independently a hydrocarbon group having 1 to 12 carbon atoms, a halogenated hydrocarbon group, or a silicon-containing hydrocarbon group, and R ¹⁴¹ and R ¹⁴² and / Or R ¹⁴³ and R ¹⁴⁴ may combine to form a divalent group, and R ¹⁴⁵ represents a hydrocarbon group having 1 to 10 carbon atoms, a silicon-containing hydrocarbon group having 1 to 10 carbon atoms, or A halogenated hydrocarbon group having 1 to 10 carbon atoms, and R ¹⁴⁶ is an aryl group having 6 to 30 carbon atoms, which may contain halogen, silicon, or a plurality of heteroelements selected therefrom. . Q ¹⁴¹ is a binding group that bridges two conjugated five-membered ring ligands, and is a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or carbon having a hydrocarbon group having 1 to 20 carbon atoms. Represents a germylene group having a hydrocarbon group of 1 to 20, M ¹⁴¹ represents zirconium or hafnium, and X ¹⁴¹ and Y ¹⁴¹ each independently represent a hydrogen atom, a halogen atom, or a carbon atom having 1 to 20 carbon atoms. Hydrogen group, alkoxy group having 1 to 20 carbon atoms, alkylamide group having 1 to 20 carbon atoms, trifluoromethanesulfonic acid group, phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or silicon-containing hydrocarbon having 1 to 20 carbon atoms Represents a group. ]

According to a fourth aspect of the present invention, in any one of the first to third aspects, the component [B] is an ion-exchange layered silicate [B-4]. A method for producing a catalyst is provided.
Furthermore, according to a fifth aspect of the present invention, there is provided an olefin polymerization catalyst according to any one of the first to fourth aspects, wherein the ion-exchange layered silicate [B-4] is a smectite group. A manufacturing method is provided.

According to a sixth aspect of the present invention, there is provided the method for producing an olefin polymerization catalyst according to any one of the first to fifth aspects, wherein M ²¹ of the component [A-2] is hafnium. Provided.
Furthermore, according to the seventh invention of the present invention, in any one of the first to sixth inventions, the olefin is prepolymerized in a weight ratio of 0.01 to 100 with respect to the component [B]. A process for producing an olefin polymerization catalyst is provided.

  According to the eighth invention of the present invention, in any one of the first to seventh inventions, the branching index (g ′) at a molecular weight (M) of 1 million (log M = 6) is 0.95 or less. Provided is a method for producing an olefin polymerization catalyst, which is used for producing an olefin polymer.

  According to the method for producing an olefin polymerization catalyst of the present invention, a propylene-based polymer containing a long-chain branch is obtained by sequentially performing specific steps using a catalyst component that produces a macromer and a catalyst component that copolymerizes the macromer. It is possible to provide a method for producing a two-way catalyst with good catalytic properties such as bulk density and flowability, which can efficiently produce a coalescence, and the activity can be improved. The highly active binary catalyst obtained by the method for producing an olefin polymerization catalyst of the present invention efficiently produces a propylene-based polymer having a large amount of long-chain branches by a simple method (for example, a single-stage polymerization method). can do. For this reason, the industrial significance of the present invention is very large.

It is a figure explaining the baseline and the section of a chromatogram in measurement of molecular weight distribution. It is a figure explaining the activity of the catalyst for olefin polymerization concerning the present invention compared with a comparative example.

The olefin polymerization catalyst according to the present invention, for example, the propylene polymerization catalyst, must contain at least the components [A-1], [A-2], [B], and [C] described later. The method for producing an olefin polymerization catalyst, for example, a propylene polymerization catalyst, is characterized by sequentially performing the following steps [I] to [III].
Step [I]: A step of producing a contact product (1) by bringing component [A-1] into contact with components [B] and [C].
Step [II]: a step of washing the contact product (1) obtained in step [I] with an inert hydrocarbon solvent so that the washing rate is 1/10 or less to produce a washed product. .
Step [III]: A step of producing a contact product (2) by bringing the component [A-2] into contact with the washed product obtained in Step [II].
Then, by carrying out propylene polymerization by single-stage polymerization in the presence of the obtained propylene polymerization catalyst, a long-chain branched propylene polymer can be produced with high activity and efficiency.
Hereinafter, the olefin polymerization catalyst, for example, the propylene polymerization catalyst and the production method thereof will be described in detail for each item.

1. Catalyst Component of Propylene Polymerization Catalyst The propylene polymerization catalyst according to the present invention must contain at least the components [A-1], [A-2], [B] and [C].

(1) Component [A-1]
Component [A-1] is a metallocene compound that forms a polymerization catalyst for producing an olefin macromer. However, a metallocene compound that forms a polymerization catalyst for generating an olefin macromer generates a propylene homopolymer having a terminal vinyl ratio (Rv) of 0.5 or more when propylene homopolymerization is performed at 70 ° C. It is a metallocene compound that forms a polymerization catalyst.
Here, the terminal vinyl ratio (Rv) is defined by the following formula.
Rv = Mn / 21000 × [Vi]
(In the formula, Mn is the number average molecular weight determined by GPC, and [Vi] is the number of terminal vinyl groups per 1000 C calculated from ¹³ C-NMR.)

Olefin macromer production will be described below.
In the polymerization of propylene, β hydrogen is generally eliminated, and a vinylidene structure terminal represented by the following structural formula (2-b) is generated. In addition, when hydrogen is used, chain transfer usually occurs preferentially to hydrogen, and a saturated terminal (isobutyl structure) as shown in the structural formula (2-c) is generated at the terminal.
However, when a complex having a special structure is used, a special chain transfer reaction generally called β-methyl elimination occurs, and the propenyl structure (vinyl structure) shown in the structural formula (2-a) is terminated. A polymer is formed (reference: Macromol. Rapid Commun. 2000, 21, 1103-1107).
In addition, when a complex having a very special structure exemplified by the present invention (a compound represented by the general formula (a1)) is used, the activity is surprisingly increased even when hydrogen is used. However, it has been found that β methyl elimination reaction preferentially occurs and the propenyl structure (vinyl structure) of the structural formula (2-a) is mainly produced.

Among the structural formulas (2-a), (2-b), and (2-c), those that can be copolymerized with a metallocene complex or a Ziegler catalyst are vinyl structures represented by the structural formula (2-a). Only. Therefore, the higher terminal vinyl ratio that can be copolymerized in all terminal structures means higher efficiency as a macromer.
Therefore, the metallocene compound capable of producing a macromer according to the present invention has a terminal vinyl ratio of a propylene homopolymer produced when propylene homopolymerization is carried out at 70 ° C., preferably 0.50 or more, preferably 0.65 or more, The metallocene compound is more preferably 0.75 or more, and ideally 1.0 (all terminals are vinyl groups).

In contrast to the β methyl elimination reaction, the terminal vinylidene structure represented by the structural formula (2-b) generated as a result of the β hydrogen elimination reaction cannot be copolymerized. Therefore, when a polymer containing a large amount of terminal vinylidene structure is used for macromer copolymerization, terminal vinylidene remains as it is, and the efficiency as a macromer is lowered. Moreover, such a low molecular weight body deteriorates mechanical properties. Further, when used as a terminal-modified raw material, the modification efficiency is poor and the functionality is lowered. Furthermore, if many vinylidene ends remain, the hue and weather resistance deteriorate.
Therefore, the metallocene compound capable of producing a macromer according to the present invention has a propylene homopolymer produced when propylene homopolymerization is performed at 70 ° C., and the terminal vinylidene ratio is less than 0.1, preferably less than 0.05. The metallocene compound is more preferably less than 0.01 and ideally 0 (substantially free of terminal vinylidene).

The starting ends after β methyl elimination reaction and β hydrogen elimination reaction are isobutyl end and n-propyl end, respectively, and become saturated hydrocarbon ends. That is, the starting end is always a saturated hydrocarbon end, and an unsaturated bond does not appear at both ends.
Here, the conditions for homopolymerization of propylene at 70 ° C. when determining the terminal vinyl ratio of the macromer complex will be described in detail.
After replacing the inside of the 3 L autoclave tank with propylene, 2.86 mL of a heptane solution of triisobutylaluminum (142 mg / mL) is added, 750 g of liquid propylene is introduced, and the temperature is raised to 70 ° C. Then, the catalyst containing a macromer complex is pumped to a polymerization tank, and polymerization is performed at 70 ° C. for 1 hour. Finally, unreacted propylene is quickly purged and the polymerization is stopped to obtain a propylene polymer for evaluating the vinyl end ratio.
The terminal vinyl ratio (Rv) and the terminal vinylidene ratio (Rvd) are the number average molecular weight obtained by GPC from 1-propenyl (vinyl) terminal concentration [Vi] obtained from ¹³ C-NMR and vinylidene terminal concentration [Vd]. As a ratio to the total number of polymer chains obtained from (Mn), it is calculated using the following formula.
Rv = (Mn / 42) × 2 × [Vi] / 1000
Rvd = (Mn / 42) × 2 × [Vd] / 1000
(However, Mn is the number average molecular weight determined by GPC.)

  Further, regarding the molecular weight (Mn) of the macromer, it is necessary to have a molecular weight higher than the entanglement molecular weight in order to show the effect of improving the melt tension when it becomes a long chain branch. Therefore, the molecular weight (Mn) of the macromer needs to be 7,500 or more, preferably 15,000 or more, more preferably 23,000 or more. With respect to the upper limit of the molecular weight (Mn) of the macromer, if the molecular weight is too high, the concentration as a macromer will decrease and the fluidity will decrease, so 200,000 or less is necessary, preferably 150,000. Hereinafter, it is more preferably 100,000 or less. Macromer molecular weight (Mn) can be controlled by selecting an optimal complex structure, using hydrogen as a molecular weight modifier, or adjusting the polymerization temperature.

Here, the detail of the measuring method of 1-propenyl (vinyl) terminal density | concentration [Vi] and vinylidene terminal density | concentration [Vd] by < ¹³ > C-NMR is as follows.
390 mg of a sample is completely dissolved in 2.5 ml of deuterated 1,1,2,2-tetrachloroethane in an NMR sample tube (10φ), and then measured at 125 ° C. by a proton complete decoupling method. The chemical shift was set to 74.2 ppm in the middle of the three peaks of deuterated 1,1,2,2-tetrachloroethane. The chemical shift of other carbon peaks is based on this.
Flip angle: 90 degrees Pulse interval: 10 seconds Resonance frequency: 100 MHz or more Integration frequency: 10,000 times or more Observation area: -20 ppm to 179 ppm

The terminal vinyl ratio (Rv) and terminal vinylidene ratio (Rvd) of this propylene-based polymer can be determined by selecting a complex having a special structure that causes the β-methyl elimination reaction selectively to the β-hydrogen elimination reaction. Control is possible.
Examples of such a complex structure include a bisindene complex having a bulky heterocyclic group at the 2-position and an aryl group which may be substituted at the 4-position.
This selectivity can also be controlled by changing the polymerization temperature. For example, in the complexes shown in the examples, the higher the polymerization temperature, the higher the terminal vinyl ratio.

The 1-propenyl (vinyl) terminal concentration [Vi] is based on the fact that carbon 1 and carbon 2 in the structural formula (2-a) are detected at 115.5 ppm and 137.6 ppm, and the vinylidene terminal concentration [Vd] uses the fact that carbon 3 and carbon 4 in the structural formula (2-b) are detected at 111.2 ppm and 144.5 ppm, respectively, Calculate as follows. Here, the total skeleton-forming carbon means all carbon atoms other than methyl carbon.
[Vi] = [peak intensity of carbon 1] / [total peak intensity of all skeleton-forming carbons] × 1000
[Vd] = [peak intensity of carbon 3] / [sum of peak intensities of all skeleton-forming carbons] × 1000

Moreover, although the value of a number average molecular weight (Mn) is obtained by gel permeation chromatography (GPC), the detail of the measuring method and a measuring instrument is as follows.
Equipment: GPC manufactured by Waters (ALC / GPC, 150C)
Detector: MIRAN, 1A, IR detector manufactured by FOXBORO (measurement wavelength: 3.42 μm)
Column: AD806M / S (3 pieces) manufactured by Showa Denko KK
Mobile phase solvent: o-dichlorobenzene (ODCB)
Measurement temperature: 140 ° C
Flow rate: 1.0 ml / min Injection volume: 0.2 ml

The sample is prepared by preparing a 1 mg / mL solution using ODCB (containing 0.5 mg / mL BHT) and dissolving it at 140 ° C. for about 1 hour.
The baseline and section of the obtained chromatogram are performed as shown in FIG.
Further, the conversion from the retention capacity obtained by GPC measurement to the molecular weight is performed using a standard curve prepared in advance by standard polystyrene. The standard polystyrenes used are all the following brands manufactured by Tosoh Corporation.
Brand: F380, F288, F128, F80, F40, F20, F10, F4, F1, A5000, A2500, A1000
Inject 0.2 mL of a solution dissolved in ODCB (containing 0.5 mg / mL BHT) so that each is 0.5 mg / mL to create a calibration curve. The calibration curve uses a cubic equation obtained by approximation by the least square method.
Viscosity formula used for conversion to molecular weight: [η] = K × M ^α uses the following numerical values.
PS: K = 1.38 × 10 ⁻⁴ , α = 0.7
PP: K = 1.03 × 10 ⁻⁴ , α = 0.78

The component [A-1] is not particularly limited as long as it is a metallocene compound that forms a macromer, and can be selected from compounds included in the general formula (a2) of the component [A-2] described later. . As a component [A-1], the following structure is mentioned as one of the non-limiting preferable embodiments.
Component [A-1] is preferably a metallocene compound represented by the following general formula (a1).

[In General Formula (a1), R ¹¹ and R ¹² each independently represent a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur. R ¹³ and R ¹⁴ each independently represent halogen, silicon, oxygen, sulfur, nitrogen, boron, phosphorus, or a C 6-16 aryl that may contain a plurality of hetero elements selected from these Or a heterocyclic group having 6 to 16 carbon atoms containing nitrogen, oxygen or sulfur. Further, M ¹¹ represents zirconium or hafnium, and X ¹¹ and Y ¹¹ each independently represent a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, or a hydrocarbon group having 1 to 20 carbon atoms. A silyl group, a halogenated hydrocarbon group having 1 to 20 carbon atoms, an amino group or an alkylamino group having 1 to 20 carbon atoms, Q ¹¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms, carbon number It represents a silylene group or a germylene group which may have 1 to 20 hydrocarbon groups. ]

R ¹¹ and R ¹² are each independently a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur, preferably a 2-furyl group, a substituted 2-furyl group, or a substituted group. The substituted 2-thienyl group or substituted 2-furfuryl group, more preferably a substituted 2-furyl group.
Moreover, as a substituted 2-furyl group, a substituted 2-thienyl group, and a substituted 2-furfuryl group, an alkyl group having 1 to 6 carbon atoms such as a methyl group, an ethyl group, and a propyl group, Examples thereof include halogen atoms such as fluorine atom and chlorine atom, alkoxy groups having 1 to 6 carbon atoms such as methoxy group and ethoxy group, and trialkylsilyl groups. Of these, a methyl group and a trimethylsilyl group are preferable, and a methyl group is particularly preferable.
Further, R ¹¹ and R ¹² are particularly preferably a 2- (5-methyl) -furyl group. R ¹¹ and R ¹² are preferably the same as each other.

R ¹³ and R ¹⁴ are halogen, silicon, oxygen, sulfur, nitrogen, boron, phosphorus, or an aryl group having 6 to 16 carbon atoms that may contain a plurality of hetero elements selected from these. In addition, as the aryl group, in the range of 6 to 16 carbon atoms, one or more hydrocarbon groups having 1 to 6 carbon atoms and trialkylsilyl groups having 1 to 6 carbon atoms on the aryl cyclic skeleton The halogen-containing hydrocarbon group having 1 to 6 carbon atoms may be substituted.
R ¹³ and R ¹⁴ may be a heterocyclic group having 6 to 16 carbon atoms containing nitrogen, oxygen or sulfur. Such a heterocyclic group is preferably a 2-furyl group, a substituted 2-furyl group, a substituted 2-thienyl group, or a substituted 2-furfuryl group, more preferably a substituted 2-furyl group. Furyl group. Examples of these substituents include alkyl groups having 1 to 6 carbon atoms such as methyl, ethyl and propyl groups, halogen atoms such as fluorine and chlorine atoms, alkoxy having 1 to 6 carbon atoms such as methoxy and ethoxy groups. Group and a trialkylsilyl group. Of these, a methyl group and a trimethylsilyl group are preferable, and a methyl group is particularly preferable.
R ¹³ and R ¹⁴ are preferably at least one of phenyl group, 4-i-propyl group, 4-trimethylsilyl group, 4-t-butylphenyl group, 2,3-dimethylphenyl group, 3,5-di- t-butylphenyl group, 4-phenyl-phenyl group, chlorophenyl group, naphthyl group, or phenanthryl group, more preferably phenyl group, 4-i-propyl group, 4-trimethylsilyl group, 4-t-butylphenyl group. 4-chlorophenyl group. R ¹³ and R ¹⁴ are preferably the same as each other.

Further, X ¹¹ and Y ¹¹ are auxiliary ligands, and react with the component [B] to generate an active metallocene having olefin polymerization ability. Therefore, as long as this object is achieved, X ¹¹ and Y ¹¹ are not limited in the type of ligand, and are independently a hydrogen atom, a halogen atom, or a hydrocarbon group having 1 to 20 carbon atoms. Represents a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, a halogenated hydrocarbon group having 1 to 20 carbon atoms, an amino group, or an alkylamino group having 1 to 20 carbon atoms.
Here, the silyl group having a hydrocarbon group having 1 to 20 carbon atoms is a trialkylsilyl group, dialkylarylsilyl group, alkyldiarylsilyl group, or triarylsilyl group having 1 to 20 carbon atoms.

Q ¹¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms, which bonds two conjugated five-membered ring ligands via carbon having 1 or 2 carbon atoms, bonding two five-membered rings, It shows either a silylene group or a germylene group which may have 1 to 20 hydrocarbon groups. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ¹¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene and 1,2-ethylene; arylalkylene groups such as diphenylmethylene; silylene groups; methylsilylene, dimethylsilylene, diethylsilylene, di Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.
Further, on an indene ring of the above general formula ^{(a1), R 12, R} 13, R 14, R 15 may have a substituent in addition. In that case, it can have a substituent at the 5- or 6-position of the indene ring. An example of such is the 5-position methyl group. As another example, substituents at the 5-position and the 6-position can be bonded to each other to form a cyclic structure. As such an example, an indacene skeleton is preferable.

Of the compounds represented by the general formula (a1), preferred compounds are specifically exemplified below.
(1) dichloro [1,1′-dimethylsilylenebis {2- (2-furyl) -4-phenyl-indenyl}] hafnium,
(2) dichloro [1,1′-dimethylsilylenebis {2- (2-thienyl) -4-phenyl-indenyl}] hafnium,
(3) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(4) dichloro [1,1′-diphenylsilylenebis {2- (5-methyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(5) Dichloro [1,1′-dimethylgermylenebis {2- (5-methyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(6) dichloro [1,1′-dimethylgermylenebis {2- (5-methyl-2-thienyl) -4-phenyl-indenyl}] hafnium,
(7) dichloro [1,1′-dimethylsilylenebis {2- (5-tert-butyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(8) dichloro [1,1′-dimethylsilylenebis {2- (5-trimethylsilyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(9) Dichloro [1,1′-dimethylsilylenebis {2- (5-phenyl-2-furyl) -4-phenyl-indenyl}] hafnium,
(10) Dichloro [1,1′-dimethylsilylenebis {2- (4,5-dimethyl-2-furyl) -4-phenyl-indenyl}] hafnium dichloride,
(11) Dichloro [1,1′-dimethylsilylenebis {2- (2-benzofuryl) -4-phenyl-indenyl}] hafnium,
(12) dichloro [1,1′-dimethylsilylenebis {2- (2-furfuryl) -4-phenyl-indenyl}] hafnium,
(13) Dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-chlorophenyl) -indenyl}] hafnium,
(14) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-fluorophenyl) -indenyl}] hafnium,
(15) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trifluoromethylphenyl) -indenyl}] hafnium,
(16) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium,
(17) Dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-i-propylphenyl) -indenyl}] hafnium,
(18) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium,
(19) Dichloro [1,1′-dimethylsilylenebis {2- (2-furyl) -4- (1-naphthyl) -indenyl}] hafnium,
(20) Dichloro [1,1′-dimethylsilylenebis {2- (2-furyl) -4- (2-naphthyl) -indenyl}] hafnium,
(21) dichloro [1,1′-dimethylsilylenebis {2- (2-furyl) -4- (2-phenanthryl) -indenyl}] hafnium,
(22) dichloro [1,1′-dimethylsilylenebis {2- (2-furyl) -4- (9-phenanthryl) -indenyl}] hafnium,
(23) Dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (1-naphthyl) -indenyl}] hafnium,
(24) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (2-naphthyl) -indenyl}] hafnium,
(25) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (2-phenanthryl) -indenyl}] hafnium,
(26) dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (9-phenanthryl) -indenyl}] hafnium,
(27) Dichloro [1,1′-dimethylsilylenebis {2- (5-tert-butyl-2-furyl) -4- (1-naphthyl) -indenyl}] hafnium,
(28) Dichloro [1,1′-dimethylsilylenebis {2- (5-tert-butyl-2-furyl) -4- (2-naphthyl) -indenyl}] hafnium,
(29) Dichloro [1,1′-dimethylsilylenebis {2- (5-tert-butyl-2-furyl) -4- (2-phenanthryl) -indenyl}] hafnium,
(30) Dichloro [1,1′-dimethylsilylenebis {2- (5-tert-butyl-2-furyl) -4- (9-phenanthryl) -indenyl}] hafnium, and the like.

  Of these, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4-phenyl-indenyl}] hafnium, dichloro [1,1′-dimethyl gel are more preferable. Mylenebis {2- (5-methyl-2-thienyl) -4-phenyl-indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- ( 4-chlorophenyl) -indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (2-naphthyl) -indenyl}] hafnium, dichloro [1, 1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-tert-butylphenyl) -indenyl}] hafnium, dichloro [1,1′- Methylsilylenebis {2- (5-methyl-2-furyl) -4- (4-i-propylphenyl) -indenyl}] hafnium, dichloro [1,1'-dimethylsilylenebis {2- (5-methyl- 2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4-biphenylyl-indenyl}] hafnium It is.

  Particularly preferred is dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4-phenyl-indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis { 2- (5-Methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-i-propylphenyl) -indenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl }] Hafnium.

Moreover, as a component [A-1], the following structure is given as another example of preferable non-limiting embodiments.
Component [A-1] is preferably a compound represented by the following general formula (a14).

[In General Formula (a14), R ^{141 to} R ¹⁴⁴ are each independently a hydrocarbon group having 1 to 12 carbon atoms, a halogenated hydrocarbon group, or a silicon-containing hydrocarbon group, and R ¹⁴¹ and R ¹⁴² and / Or R ¹⁴³ and R ¹⁴⁴ may combine to form a divalent group, and R ¹⁴⁵ represents a hydrocarbon group having 1 to 10 carbon atoms, a silicon-containing hydrocarbon group having 1 to 10 carbon atoms, or A halogenated hydrocarbon group having 1 to 10 carbon atoms, and R ¹⁴⁶ is an aryl group having 6 to 30 carbon atoms, which may contain halogen, silicon, or a plurality of heteroelements selected therefrom. . Q ¹⁴¹ is a binding group that bridges two conjugated five-membered ring ligands, and is a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or carbon having a hydrocarbon group having 1 to 20 carbon atoms. Represents a germylene group having a hydrocarbon group of 1 to 20, M ¹⁴¹ represents zirconium or hafnium, and X ¹⁴¹ and Y ¹⁴¹ each independently represent a hydrogen atom, a halogen atom, or a carbon atom having 1 to 20 carbon atoms. Hydrogen group, alkoxy group having 1 to 20 carbon atoms, alkylamide group having 1 to 20 carbon atoms, trifluoromethanesulfonic acid group, phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or silicon-containing hydrocarbon having 1 to 20 carbon atoms Represents a group. ]

In the above formula, Q ¹⁴¹ is a binding group that bridges two conjugated five-membered ring ligands, and has a divalent hydrocarbon group having 1 to 20 carbon atoms and a hydrocarbon group having 1 to 20 carbon atoms. A silylene group or a germylene group having a hydrocarbon group having 1 to 20 carbon atoms, preferably a substituted silylene group or a substituted germylene group. The substituent bonded to silicon and germanium is preferably a hydrocarbon group having 1 to 12 carbon atoms, and two substituents may be linked.
Specific examples include methylene, dimethylmethylene, ethylene-1,2-diyl, dimethylsilylene, diethylsilylene, diphenylsilylene, methylphenylsilylene, 9-silafluorene-9,9-diyl, dimethylsilylene, diethylsilylene, Examples thereof include diphenylsilylene, methylphenylsilylene, 9-silafluorene-9,9-diyl, dimethylgermylene, diethylgermylene, diphenylgermylene, methylphenylgermylene and the like.

In the above formula, M ¹⁴¹ is zirconium or hafnium, preferably hafnium.
X ¹⁴¹ and Y ¹⁴¹ are auxiliary ligands, and react with the cocatalyst of component [B] to generate an active metallocene having an olefin polymerization ability. Therefore, as long as this object is achieved, X ¹⁴¹ and Y ¹⁴¹ are not limited in the type of ligand, and are independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, An alkoxy group having 1 to 20 carbon atoms, an alkylamide group having 1 to 20 carbon atoms, a trifluoromethanesulfonic acid group, a phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms is shown. .

R ^{141 to} R ¹⁴⁴ are each independently a hydrocarbon group or halogenated hydrocarbon having 1 to 12 carbon atoms, preferably 1 to 10 carbon atoms, more preferably 1 to 8 carbon atoms, and particularly preferably 1 to 6 carbon atoms. Group or a silicon-containing hydrocarbon group.
Specific examples of the hydrocarbon group represented by R ^{141 to} R ¹⁴⁴ include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, s-butyl, t-butyl, n-pentyl, n -In addition to alkyl groups such as hexyl, cyclopropyl, cyclopentyl and cyclohexyl, and alkenyl groups such as vinyl, propenyl and cyclohexenyl, phenyl groups and the like can be mentioned.
Specific examples of the silicon-containing hydrocarbon group represented by R ^{141 to} R ¹⁴⁴ include trialkylsilyl groups such as trimethylsilyl, triethylsilyl, and t-butyldimethylsilyl.
In addition, the halogenated hydrocarbon group represented by R ^{141 to} R ¹⁴⁴ is a group in which a halogen atom is substituted at an arbitrary position of the hydrocarbon group, and the halogen atom is a fluorine atom, a chlorine atom, a bromine atom, or an iodine atom. Any of these may be used. Specific examples thereof include fluoromethyl, difluoromethyl, trifluoromethyl, chloromethyl, dichloromethyl, trichloromethyl, 2-fluorophenyl, 3-fluorophenyl, 4-fluorophenyl, 4-chlorophenyl, and 3,5-difluorophenyl. 2,6-difluorophenyl, 2,4-dichlorophenyl, 3,5-dichlorophenyl, 2,6-dichlorophenyl, 2,5-dichlorophenyl, 2,4,6-trifluorophenyl, pentafluorophenyl and the like.
Further, as a preferred example, R ^{141 to} R ¹⁴⁴ are all the same hydrocarbon group, and particularly preferably a methyl group.

When R ¹⁴¹ and R ¹⁴² and / or R ¹⁴³ and R ¹⁴⁴ are combined to form a divalent group, the carbon number is usually 3 or more, preferably 4 or more, and usually 9 or less, preferably 6 or less. As the kind of divalent group, a hydrocarbon group is preferable. Specific examples of the divalent hydrocarbon group include dimethylene, trimethylene, tetramethylene, heptamethylene, hexamethylene, heptamethylene, octamethylene, nonamethylene, trimethylene, tetramethylene and heptamethylene are preferred, and tetramethylene is particularly preferred. preferable.
Furthermore, it is preferable that any one of R ¹⁴¹ and R ¹⁴² or R ¹⁴³ and R ¹⁴⁴ forms a divalent group rather than a divalent group.

R ¹⁴⁵ is a hydrocarbon group having 1 to 10 carbon atoms, a silicon-containing hydrocarbon group having 1 to 10 carbon atoms, or a halogenated hydrocarbon group having 1 to 10 carbon atoms, preferably 3 to 3 carbon atoms. 9 hydrocarbon group, a silicon-containing hydrocarbon group having 3 to 9 carbon atoms, or a halogenated hydrocarbon group having 3 to 9 carbon atoms, more preferably a hydrocarbon having 3 to 6 carbon atoms having a branched structure. It is a group. Moreover, when it has a branched structure, it is preferable that the α position is a branch as the branch position. The branched structure is preferably secondary carbon.
Specific preferred examples of R ¹⁴⁵ include i-propyl, sec-butyl, iso-butyl, t-butyl, 2-pentyl, 3-methyl-2-butyl, 2-hexyl, and 3-methyl-2-pentyl. 4-methyl-2-pentyl, cyclohexyl, phenyl and the like, particularly preferably i-propyl.

R ¹⁴⁶ is an aryl group having 6 to 30 carbon atoms, preferably 6 to 24 carbon atoms, which may contain halogen, silicon, or a plurality of hetero elements selected from these.
Preferred examples of R ¹⁴⁶ include phenyl, 3-chlorophenyl, 4-chlorophenyl, 3-fluorophenyl, 4-fluorophenyl, 4-methylphenyl, 4-i-propylphenyl, 4-t-butylphenyl, 4-trimethylsilyl. Phenyl, 4- (2-fluorobiphenylyl), 4- (2-chlorobiphenylyl), 1-naphthyl, 2-naphthyl, 3,5-dimethyl-4-tert-butylphenyl, 3,5-dimethyl-4 -Trimethylsilylphenyl and the like.

Examples of the metallocene compound include, for example, the following compounds, but the present invention is not limited to these compounds.
(Abbreviation: OHFlu: 1,2,3,4,5,6,7,8-octahydro-9-fluorenyl. TMCp: 2,3,4,5-tetramethylcyclopentadienyl. Azu: 4H-1- Azulenyl. THAzu: 5,6,7,8-tetrahydro-4H-1-azurenyl.)
(1) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4-phenyl-Azu)] hafnium,
(2) dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium,
(3) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-fluorophenyl) -Azu)] hafnium,
(4) dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (3-chlorophenyl) -Azu)] hafnium,
(5) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (3-fluorophenyl) -Azu)] hafnium,
(6) dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-methylphenyl) -Azu)] hafnium,
(7) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-i-propylphenyl) -Azu)] hafnium,
(8) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-t-butylphenyl) -Azu)] hafnium,
(9) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4-trimethylsilylphenyl) -Azu)] hafnium,
(10) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4- (2-fluorobiphenylyl))-Azu)] hafnium,
(11) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4- (2-chlorobiphenylyl))-Azu)] hafnium,
(12) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (4- (2-chlorobiphenylyl))-Azu)] hafnium,
(13) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (1-naphthyl) -Azu)] hafnium,
(14) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (2-naphthyl) -Azu)] hafnium,
(15) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (3,5-dimethyl-4-tert-butylphenyl) -Azu)] hafnium,
(16) Dichloro [dimethylsilylene (OHFlu) (2-i-propyl-4- (3,5-dimethyl-4-trimethylsilylphenyl) -Azu)] hafnium,
(17) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4-phenyl-Azu)] hafnium,
(18) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4- (4-chlorophenyl) -Azu)] hafnium,
(19) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4- (4-fluorophenyl) -Azu)] hafnium,
(20) Dichloro [dimethylsilylene (OHFlu) (2-cyclohexyl-4-phenyl-Azu)] hafnium,

(21) Dichloro [dimethylsilylene (OHFlu) (2-cyclohexyl-4- (4-chlorophenyl) -Azu)] hafnium,
(22) Dichloro [dimethylsilylene (OHFlu) (2-cyclohexyl-4- (4-fluorophenyl) -Azu)] hafnium,
(23) Dichloro [dimethylsilylene (OHFlu) (2-phenyl-4-phenyl-Azu)] hafnium,
(24) Dichloro [dimethylsilylene (OHFlu) (2-phenyl-4- (4-chlorophenyl) -Azu)] hafnium,
(25) Dichloro [dimethylsilylene (OHFlu) (2-phenyl-4- (4-fluorophenyl) -Azu)] hafnium,
(26) Dichloro [dimethylsilylene (OHFlu) (2-sec-pentyl-4- (4-chlorophenyl) -Azu)] hafnium,
(27) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4- (4-t-butylphenyl) -Azu)] hafnium,
(28) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4- (4-trimethylsilylphenyl) -Azu)] hafnium,
(29) Dichloro [dimethylsilylene (OHFlu) (2-sec-butyl-4- (4- (2-fluorobiphenylyl))-Azu)] hafnium,
(30) Dichloro [dimethylsilylene (2,7-di-t-butyl-OHFlu) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium,
(31) Dichloro [dimethylsilylene (2,7-di-t-butyl-OHFlu) (2-i-propyl-4-phenyl-Azu)] hafnium,
(32) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4-phenyl-Azu)] hafnium,
(33) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium,
(34) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-fluorophenyl) -Azu)] hafnium,
(35) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3-chlorophenyl) -Azu)] hafnium,
(36) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3-fluorophenyl) -Azu)] hafnium,
(37) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-methylphenyl) -Azu)] hafnium,
(38) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-i-propylphenyl) -Azu)] hafnium,
(39) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-t-butylphenyl) -Azu)] hafnium,
(40) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-trimethylsilylphenyl) -Azu)] hafnium,

(41) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4- (2-fluorobiphenylyl))-Azu)] hafnium,
(42) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4- (2-chlorobiphenylyl))-Azu)] hafnium,
(43) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (1-naphthyl) -Azu)] hafnium,
(44) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (2-naphthyl) -Azu)] hafnium,
(45) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3,5-dimethyl-4-tert-butylphenyl) -Azu)] hafnium,
(46) Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3,5-dimethyl-4-trimethylsilylphenyl) -Azu)] hafnium,
(47) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4-phenyl-Azu)] hafnium,
(48) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4- (4-chlorophenyl) -Azu)] hafnium,
(49) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4- (4-fluorophenyl) -Azu)] hafnium,
(50) Dichloro [dimethylsilylene (TMCp) (2-cyclohexyl-4-phenyl-Azu)] hafnium,
(51) Dichloro [dimethylsilylene (TMCp) (2-cyclohexyl-4- (4-chlorophenyl) -Azu)] hafnium,
(52) Dichloro [dimethylsilylene (TMCp) (2-cyclohexyl-4- (4-fluorophenyl) -Azu)] hafnium,
(53) Dichloro [dimethylsilylene (TMCp) (2-phenyl-4-phenyl-Azu)] hafnium,
(54) Dichloro [dimethylsilylene (TMCp) (2-phenyl-4- (4-chlorophenyl) -Azu)] hafnium,
(55) Dichloro [dimethylsilylene (TMCp) (2-phenyl-4- (4-fluorophenyl) -Azu)] hafnium,
(56) Dichloro [dimethylsilylene (TMCp) (2-sec-pentyl-4- (4-chlorophenyl) -Azu)] hafnium,
(57) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4- (4-t-butylphenyl) -Azu)] hafnium,
(58) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4- (4-trimethylsilylphenyl) -Azu)] hafnium,
(59) Dichloro [dimethylsilylene (TMCp) (2-sec-butyl-4- (4- (2-fluorobiphenylyl))-Azu)] hafnium,
(60) Dichloro [dimethylmethylene (TMCp) (2-i-propyl-4-phenyl-Azu)] hafnium,

(61) Dichloro [dimethylmethylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium (62) Dichloro [diphenylsilylene (TMCp) (2-i-propyl-4-phenyl- Azu)] hafnium (63) dichloro [diphenylsilylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium (64) dichloro [diphenylsilylene (TMCp) (2-i-propyl- 4-phenyl-Azu)] hafnium (65) dichloro [diphenylsilylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium (66) dichloro [dimethylgermylene (TMCp) (2 -I-propyl-4-phenyl-Azu)] hafnium (67) dichloro [Dimethylgermylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium (68) dichloro [dimethylgermylene (TMCp) (2-i-propyl-4- (4-t -Butylphenyl) -Azu)] hafnium, and the like.

In order to use a C1 symmetrical transition metal compound as the polymerization catalyst component as the component [A-1] according to the present invention, among the transition metal compounds of the above (1) to (68), dichloro [dimethylsilylene (TMCp ) (2-i-propyl-4-phenyl-Azu)] hafnium, dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-chlorophenyl) -Azu)] hafnium, dichloro [dimethylsilylene (TMCp) ) (2-i-propyl-4- (3-chlorophenyl) -Azu)] hafnium, dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3-fluorophenyl) -Azu)] hafnium, dichloro [Dimethylsilylene (TMCp) (2-i-propyl-4- (4-t-butylphenyl) -Azu)] hafni Dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4-trimethylsilylphenyl) -Azu)] hafnium, dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (4- ( 2-fluorobiphenylyl))-Azu)] hafnium, dichloro [dimethylsilylene (TMCp) (2-i-propyl-4- (3,5-dimethyl-4-tert-butylphenyl) -Azu)] hafnium, dichloro [Dimethylsilylene (TMCp) (2-i-propyl-4- (3,5-dimethyl-4-trimethylsilylphenyl) -Azu)] hafnium is preferred.
A compound in which the central metal M in the transition metal compounds (1) to (68) exemplified above is replaced by zirconium instead of hafnium can also be used as the polymerization catalyst component.

(2) Component [A-2]
Component [A-2] is a metallocene compound represented by the following general formula (a2).

[In General Formula (a2), E ²¹ and E ²² are each independently a cyclopentadienyl group, an indenyl group, a fluorenyl group, or an azulenyl group, and each may have a substituent (provided that The substituent is not a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur.) Q ²¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or a germylene group optionally having a hydrocarbon group having 1 to 20 carbon atoms, and M ²¹ represents zirconium or hafnium. , X ²¹ and Y ²¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogen having 1 to 20 carbon atoms. Represents a hydrocarbyl group, an amino group, or an alkylamino group having 1 to 20 carbon atoms. ]

E ²¹ and E ²² are each independently a cyclopentadienyl group, an indenyl group, a fluorenyl group, or an azulenyl group, and each may have a substituent. The substituent is not a C 4-16 heterocyclic group containing nitrogen, oxygen or sulfur.
Of these, a substituted cyclopentadienyl group, a substituted indenyl group, and a substituted azulenyl group are preferable.

Component [A-2] is preferably a compound that forms a polymerization catalyst capable of copolymerizing an olefin monomer and an olefin macromer. Such a compound may be a compound that simultaneously forms a catalyst capable of producing a macromer.
As a non-limiting preferable example of component [A-2], when E ²¹ and E ²² are substituted cyclopentadienyl groups, the following structures can be exemplified.

[In General Formula (a3), R ³¹ and R ³⁴ each independently represent an aliphatic hydrocarbon group having 1 to 6 carbon atoms, and R ³² and R ³⁵ each independently represent 1 to C carbon atoms. 6 and R ³³ and R ³⁶ each independently represents a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms. X ³¹ and Y ³¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogenated group having 1 to 20 carbon atoms. Represents a hydrocarbon group, an amino group, or an alkylamino group having 1 to 20 carbon atoms, and Q ³¹ has a divalent hydrocarbon group having 1 to 20 carbon atoms and a hydrocarbon group having 1 to 20 carbon atoms. Represents a silylene group or a germylene group, and M ³¹ represents zirconium or hafnium. ]

R ³¹ and R ³⁴ are each independently an aliphatic hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group having 1 to 4 carbon atoms.
Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, n-pentyl, i-pentyl, n-hexyl, and preferably methyl. , Ethyl and n-propyl, particularly preferably a methyl group.
R ³² and R ³⁵ are each independently a hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group, more preferably an alkyl group having 1 to 4 carbon atoms, and particularly preferably methyl. It is a group.
Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, t-butyl, n-pentyl, i-pentyl, n-hexyl, phenyl and the like. Preferred are methyl, ethyl, n-propyl, i-propyl, t-butyl and phenyl.
R ³³ and R ³⁶ are each independently a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group, more preferably an alkyl group having 1 to 4 carbon atoms, A methyl group is preferred.
Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, t-butyl, n-pentyl, i-pentyl, n-hexyl, phenyl and the like. Preferred are methyl, ethyl, n-propyl, i-propyl, t-butyl and phenyl.

In the general formula (a3), X ³¹ and Y ³¹ are auxiliary ligands, and react with the component [B] as a cocatalyst to generate an active metallocene having an olefin polymerization ability. As this object is achieved, X ³¹ and Y ³¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, A halogenated hydrocarbon group having 1 to 20 carbon atoms, an amino group, or an alkylamino group having 1 to 20 carbon atoms is represented.
Here, the silyl group having a hydrocarbon group having 1 to 20 carbon atoms is a trialkylsilyl group, dialkylarylsilyl group, alkyldiarylsilyl group, or triarylsilyl group having 1 to 20 carbon atoms.

In general formula (a3), Q ³¹ is a divalent valence having 1 to 20 carbon atoms that bridges two conjugated five-membered ring ligands via carbon having 1 or 2 carbon atoms, which bonds two five-membered rings. Or a silylene group or a germylene group which may have a hydrocarbon group having 1 to 20 carbon atoms. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ³¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene and 1,2-ethylene; arylalkylene groups such as diphenylmethylene; silylene groups; methylsilylene, dimethylsilylene, diethylsilylene, di Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.

Among the compounds represented by the general formula (a3),
(1) dichloro {dimethylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium,
(2) dichloro {diphenylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium,
(3) dichloro {dimethylgermylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium,
(4) dichloro {dimethylsilylenebis (2,5-dimethyl-3-phenylcyclopentadienyl)} hafnium,
(5) dichloro {dimethylsilylenebis (2-ethyl-3-phenyl-5-methylcyclopentadienyl)} hafnium,
(6) dichloro {dimethylsilylenebis (2,3,5-triethylcyclopentadienyl)} hafnium,
(7) dichloro {dimethylsilylenebis (2,5-dimethyl-3-ethylcyclopentadienyl)} hafnium,
(8) dichloro {dimethylsilylenebis (2,3-dimethyl-5-ethylcyclopentadienyl)} hafnium,
(9) Dichloro {dimethylsilylenebis (2,5-dimethyl-3-i-propylcyclopentadienyl)} hafnium,
(10) dichloro {dimethylsilylenebis (2,4-dimethylcyclopentadienyl)} hafnium,
More preferably, dichloro {dimethylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium, dichloro {diphenylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium, dichloro {dimethylgel Mylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium, dichloro {dimethylsilylenebis (2,5-dimethyl-3-phenylcyclopentadienyl)} hafnium, dichloro {dimethylsilylenebis (2,4 -Dimethylcyclopentadienyl)} hafnium.

Moreover, as a non-limiting preferable example of component [A-2], when E ²¹ and E ²² are substituted indenyl groups, the following structures can be exemplified.

[In General Formula (a4), R ⁴¹ and R ⁴³ are each independently an aliphatic hydrocarbon group having 1 to 6 carbon atoms, and R ⁴² and R ⁴⁴ are each independently halogen, silicon, Or it is a C6-C30 aryl group which may contain the some hetero element selected from these. X ⁴¹ and Y ⁴¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogenated group having 1 to 20 carbon atoms. Represents a hydrocarbon group, an amino group or an alkylamino group having 1 to 20 carbon atoms, and Q ⁴¹ has a divalent hydrocarbon group having 1 to 20 carbon atoms and a hydrocarbon group having 1 to 20 carbon atoms. It represents also silylene group or a germylene group, M ⁴¹ represents zirconium or hafnium. ]

R ⁴¹ and R ⁴³ are each independently an aliphatic hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group having 1 to 4 carbon atoms.
Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, n-pentyl, i-pentyl, n-hexyl, and preferably methyl. , Ethyl, n-propyl, i-propyl.
R ⁴² and R ⁴⁴ are halogen, silicon, or an aryl group having 6 to 30 carbon atoms that may contain a plurality of heteroelements selected from these. As the aryl group, In the range of 6 to 16 carbon atoms, one or more hydrocarbon groups having 1 to 6 carbon atoms, trialkylsilyl groups having 1 to 6 carbon atoms, and halogens having 1 to 6 carbon atoms on the aryl cyclic skeleton You may have a hydrocarbon group as a substituent.
At least one of R ⁴² and R ⁴⁴ is preferably a phenyl group, 4-i-propyl group, 4-trimethylsilyl group, 4-t-butylphenyl group, 2,3-dimethylphenyl group, 3,5-di- t-butylphenyl group, 4-phenyl-phenyl group, chlorophenyl group, naphthyl group, or phenanthryl group, more preferably phenyl group, 4-i-propyl group, 4-trimethylsilyl group, 4-t-butylphenyl group. 4-chlorophenyl group. R ⁴² and R ⁴⁴ are preferably the same as each other.

Furthermore, X ⁴¹ and Y ⁴¹ are auxiliary ligands, and react with the component [B] to generate an active metallocene having olefin polymerization ability. As this object, X ¹ and Y ¹ are independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, carbon A halogenated hydrocarbon group having 1 to 20 amino acids, an amino group or an alkylamino group having 1 to 20 carbon atoms is represented.
Here, the silyl group having a hydrocarbon group having 1 to 20 carbon atoms is a trialkylsilyl group, dialkylarylsilyl group, alkyldiarylsilyl group, or triarylsilyl group having 1 to 20 carbon atoms.
Q ⁴¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms that connects two five-membered rings and bridges two conjugated five-membered ring ligands through one or two carbon atoms; It shows either a silylene group or a germylene group which may have a hydrocarbon group having 1 to 20 carbon atoms. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ⁴¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene, 1,2-ethylene, etc .; arylalkylene groups such as diphenylmethylene; silylene groups; methylsilylene, dimethylsilylene, diethylsilylene, diethylene Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.

Among these compounds represented by the general formula (a4),
(1) dichloro {1,1′-dimethylsilylenebis (2-methyl-4-phenylindenyl)} hafnium,
(2) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) indenyl}] hafnium,
(3) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-t-butylphenyl) indenyl}] hafnium,
(4) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-trimethylsilylphenyl) indenyl}] hafnium,
(5) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-chloro-4-tert-butylphenyl) indenyl}] hafnium,
(6) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-methyl-4-tert-butylphenyl) indenyl}] hafnium,
(7) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-chloro-4-trimethylsilylphenyl) indenyl}] hafnium,
(8) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-methyl-4-trimethylsilylphenyl) indenyl}] hafnium,
(9) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (1-naphthyl) indenyl}] hafnium,
(10) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-naphthyl) indenyl}] hafnium,
(11) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-fluoro-4-biphenyl) indenyl}] hafnium,
(12) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-chloro-4-biphenyl) indenyl}] hafnium,
(13) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (9-phenanthryl) indenyl}] hafnium,
(14) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chloro-2-naphthyl) indenyl}] hafnium,
(15) Dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (4-chlorophenyl) indenyl}] hafnium,
(16) Dichloro [1,1′-dimethylsilylenebis {2-n-propyl-4- (3-chloro-4-trimethylsilylphenyl) indenyl}] hafnium,
(17) Dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (3-chloro-4-tert-butylphenyl) indenyl}] hafnium,
(18) dichloro [1,1′-dimethylgermylenebis {2-methyl-4- (2-fluoro-4-biphenyl) indenyl}] hafnium,
(19) Dichloro [1,1′-dimethylgermylenebis {2-methyl-4- (4-t-butylphenyl) indenyl}] hafnium,
(20) Dichloro [1,1 ′-(9-silafluorene-9,9-diyl) bis {2-ethyl-4- (4-chlorophenyl) indenyl}] hafnium.

Moreover, as a non-limiting preferable example of component [A-2], when E ²¹ and E ²² are substituted azulenyl groups, the following structures can be exemplified.

[In General Formula (a5), R ⁵¹ and R ⁵² are each independently a hydrocarbon group having 1 to 6 carbon atoms. R ⁵³ and R ⁵⁴ are each independently a halogen atom, silicon, or an aryl group having 6 to 30 carbon atoms which may contain a plurality of hetero elements selected from these. Q ⁵¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or a germylene group which may have a hydrocarbon group having 1 to 20 carbon atoms, and M ⁵¹ represents zirconium or hafnium. , X ⁵¹ and Y ⁵¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogen having 1 to 20 carbon atoms. Represents a hydrocarbyl group, an amino group, or an alkylamino group having 1 to 20 carbon atoms. ]

R ⁵¹ and R ⁵² are each independently a hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group, and more preferably an alkyl group having 1 to 4 carbon atoms. Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, n-pentyl, i-pentyl, n-hexyl, and preferably methyl. , Ethyl, n-propyl.

R ⁵³ and R ⁵⁴ each independently contain halogen, silicon, or a plurality of heteroelements selected from these, having 6 to 30 carbon atoms, preferably 6 to 24 carbon atoms. Of the aryl group. Such an aryl group is a phenyl group, a biphenylyl group, or a naphthyl group which may have a substituent. Preferable examples include phenyl, 3-chlorophenyl, 4-chlorophenyl, 3-fluorophenyl, 4-fluorophenyl, 4-methylphenyl, 4-i-propylphenyl, 4-t-butylphenyl, 4-trimethylsilylphenyl, 4 -(2-fluoro-4-biphenylyl), 4- (2-chloro-4-biphenylyl), 1-naphthyl, 2-naphthyl, 4-chloro-2-naphthyl, 3-methyl-4-trimethylsilylphenyl, 3, Examples include 5-dimethyl-4-t-butylphenyl, 3,5-dimethyl-4-trimethylsilylphenyl, 3,5-dichloro-4-trimethylsilylphenyl, and the like.

X ⁵¹ and Y ⁵¹ are auxiliary ligands that react with the component [B] as a co-catalyst to generate an active metallocene having olefin polymerization ability. Therefore, as long as this object is achieved, X ⁵¹ and Y ⁵¹ are not limited in the type of ligand, and are independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, An alkoxy group having 1 to 20 carbon atoms, an alkylamide group having 1 to 20 carbon atoms, a trifluoromethanesulfonic acid group, a phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms. Show.

Q ⁵¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms which bonds two conjugated five-membered ligands via carbon having 1 or 2 carbon atoms, which bonds two five-membered rings, It shows either a silylene group or a germylene group which may have 1 to 20 hydrocarbon groups. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ⁵¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene, 1,2-ethylene, arylalkylene groups such as diphenylmethylene, silylene groups, methylsilylene, dimethylsilylene, diethylsilylene, diethylene. Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.
Further, M ⁵¹ is zirconium or hafnium, preferably hafnium.

Non-limiting examples of the metallocene compound represented by the general formula (a5) include the following.
However, only representative exemplary compounds are described avoiding many complicated examples. Moreover, although the compound in which the central metal is hafnium has been described, it is obvious that the same zirconium compound can be used, and various ligands, cross-linking groups, or auxiliary ligands can be arbitrarily used.
(1) dichloro {1,1′-dimethylsilylenebis (2-methyl-4-phenyl-4-hydroazurenyl)} hafnium,
(2) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium,
(3) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-tert-butylphenyl) -4-hydroazurenyl}] hafnium,
(4) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium,
(5) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-chloro-4-tert-butylphenyl) -4-hydroazurenyl}] hafnium,
(6) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-methyl-4-tert-butylphenyl) -4-hydroazurenyl}] hafnium,
(7) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-chloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium,
(8) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (3-methyl-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium,
(9) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (1-naphthyl) -4-hydroazurenyl}] hafnium,
(10) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-naphthyl) -4-hydroazurenyl}] hafnium,
(11) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chloro-2-naphthyl) -4-hydroazurenyl}] hafnium,
(12) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-fluoro-4-biphenylyl) -4-hydroazurenyl}] hafnium,
(13) Dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (2-chloro-4-biphenylyl) -4-hydroazurenyl}] hafnium,
(14) dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (9-phenanthryl) -4-hydroazurenyl}] hafnium,
(15) Dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium,
(16) dichloro [1,1′-dimethylsilylenebis {2-n-propyl-4- (3-chloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium,
(17) dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (3-chloro-4-tert-butylphenyl) -4-hydroazurenyl}] hafnium,
(18) dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (3-methyl-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium,
(19) Dichloro [1,1′-dimethylgermylenebis {2-methyl-4- (2-fluoro-4-biphenylyl) -4-hydroazurenyl}] hafnium,
(20) Dichloro [1,1′-dimethylgermylenebis {2-methyl-4- (4-tert-butylphenyl) -4-hydroazurenyl}] hafnium,
(21) Dichloro [1,1 ′-(9-silafluorene-9,9-diyl) bis {2-ethyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium,
(22) dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (4-chloro-2-naphthyl) -4-hydroazurenyl}] hafnium,
(23) dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (2-fluoro-4-biphenylyl) -4-hydroazurenyl}] hafnium,
(24) dichloro [1,1 ′-(9-silafluorene-9,9-diyl) bis {2-ethyl-4- (3,5-dichloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium, Etc.

  Of these, dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2- Methyl-4- (3-chloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (2-fluoro-4-biphenylyl) -4 -Hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (4-chloro-2-naphthyl) -4-hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2-Ethyl-4- (3-methyl-4-trimethylsilylphenyl) -4-hydroazurenyl}] ha Dichloro, [1,1 ′-(9-silafluorene-9,9-diyl) bis {2-ethyl-4- (3,5-dichloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] hafnium, is there.

  Particularly preferably, dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2-ethyl -4- (2-Fluoro-4-biphenylyl) -4-hydroazurenyl}] hafnium, dichloro [1,1′-dimethylsilylenebis {2-ethyl-4- (3-methyl-4-trimethylsilylphenyl) -4- Hydroazurenyl}] hafnium, dichloro [1,1 ′-(9-silafluorene-9,9-diyl) bis {2-ethyl-4- (3,5-dichloro-4-trimethylsilylphenyl) -4-hydroazurenyl}] Hafnium.

Moreover, as a non-limiting preferable example of component [A-2], when E ²¹ and E ²² are a cyclopentadienyl group and an azulenyl group, the following structures can be exemplified.

In the general formula (a6), R ⁶¹ is a hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group, more preferably an alkyl group having 1 to 4 carbon atoms. Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, n-pentyl, i-pentyl, n-hexyl, and preferably methyl. , Ethyl, n-propyl.
R ⁶² is an aryl group having 6 to 30 carbon atoms, preferably 6 to 24 carbon atoms, which may contain halogen, silicon, or a plurality of hetero elements selected from these. Such an aryl group is a phenyl group, a biphenylyl group, or a naphthyl group which may have a substituent.
Preferable examples include phenyl, 3-chlorophenyl, 4-chlorophenyl, 3-fluorophenyl, 4-fluorophenyl, 4-methylphenyl, 4-i-propylphenyl, 4-t-butylphenyl, 4-trimethylsilylphenyl, 4 -(2-fluoro-4-biphenylyl), 4- (2-chloro-4-biphenylyl), 1-naphthyl, 2-naphthyl, 4-chloro-2-naphthyl, 3-methyl-4-trimethylsilylphenyl, 3, Examples include 5-dimethyl-4-t-butylphenyl, 3,5-dimethyl-4-trimethylsilylphenyl, 3,5-dichloro-4-trimethylsilylphenyl, and the like.
R ⁶³ , R ⁶⁴ , R ⁶⁵ and R ⁶⁶ are each independently a hydrogen atom or a hydrocarbon group having 1 to 6 carbon atoms. Specific examples include methyl, ethyl, n-propyl, Examples include i-propyl, n-butyl, i-butyl, sec-butyl, t-butyl, n-pentyl, i-pentyl, n-hexyl, phenyl and the like, preferably methyl, ethyl, n-propyl, i- Propyl, t-butyl, phenyl.
However, any two or more of R ⁶³ , R ⁶⁴ , R ⁶⁵ and R ⁶⁶ are substituents other than hydrogen atoms, and any one or more of R ⁶³ , R ⁶⁴ , R ⁶⁵ and R ⁶⁶ are hydrogen Is an atom.

X ⁶¹ and Y ⁶¹ are auxiliary ligands that react with the component [B] as a co-catalyst to generate an active metallocene having olefin polymerization ability. As this object is achieved, X ¹ and Y ¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, or 1 to 20 carbon atoms. An alkylamide group, a trifluoromethanesulfonic acid group, a phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms.
Q ⁶¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms that bonds two conjugated five-membered ring ligands via carbon having 1 or 2 carbon atoms, which bonds two five-membered rings, It shows either a silylene group or a germylene group which may have a hydrocarbon group having 1 to 20 carbon atoms. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ⁶¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene and 1,2-ethylene; arylalkylene groups such as diphenylmethylene; silylene groups; methylsilylene, dimethylsilylene, diethylsilylene, diethylene Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.
Further, M ⁶¹ is zirconium or hafnium, preferably hafnium.

Among the compounds represented by the general formula (a6),
(1) dichloro {1,1′-dimethylsilylene (2,3-dimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(2) dichloro {1,1′-dimethylsilylene (3,4-dimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(3) dichloro {1,1′-dimethylsilylene (2,5-dimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(4) dichloro {1,1′-dimethylsilylene (2,3-di-t-butylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(5) dichloro {1,1′-dimethylsilylene (3,4-di-t-butylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(6) dichloro {1,1′-dimethylsilylene (2,5-di-t-butylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(7) dichloro {1,1′-dimethylsilylene (2,3-diphenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(8) dichloro {1,1′-dimethylsilylene (3,4-diphenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(9) dichloro {1,1′-dimethylsilylene (2,5-diphenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(10) dichloro {1,1′-dimethylsilylene (2-methyl-4-ethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(11) dichloro {1,1′-dimethylsilylene (2-ethyl-4-methylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(12) dichloro {1,1′-dimethylsilylene (2-methyl-4-tert-butylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(13) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(14) dichloro {1,1′-dimethylsilylene (2,3,4-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(15) dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(16) dichloro {1,1′-dimethylsilylene (2,3-dimethyl-4-phenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(17) dichloro {1,1′-dimethylsilylene (2,3-dimethyl-5-phenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(18) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-ethyl-4-phenyl-4H-azurenyl)} hafnium,
(19) dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-ethyl-4-phenyl-4H-azurenyl)} hafnium,
(20) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (4-phenyl-2-i-propyl-4H-azurenyl)} hafnium,

(21) Dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-i-propyl-4-t-phenyl-2-i-propyl-4H-azurenyl)} hafnium ,
(22) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4- (4-chlorophenyl) -2-methyl-4H-azurenyl)} hafnium,
(23) dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-methyl-4- (4-chlorophenyl) -2-methyl-4H-azurenyl)} hafnium,
(24) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4- (3-methylphenyl) -4H-azulenyl)} hafnium,
(25) dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-methyl-4- (3-methylphenyl) -4H-azurenyl)} hafnium,
(26) Dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4- (4-t-butylphenyl) -2-methyl-4H-azurenyl)} hafnium,
(27) Dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-methyl-4- (4-tert-butylphenyl) -2-methyl-4H-azurenyl)} hafnium,
(28) dichloro {1,1′-dimethylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4- (2-naphthyl) -4H-azulenyl)} hafnium,
(29) dichloro {1,1′-dimethylsilylene (2,4,5-trimethylcyclopentadienyl) (2-methyl-4- (2-naphthyl) -4H-azulenyl)} hafnium,
(30) dichloro {1,1′-methylphenylsilylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(31) dichloro {1,1′-silacyclobutenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(32) dichloro {1,1′-silacyclopropenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(33) dichloro {1,1′-silafluorenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(34) dichloro {1,1′-methylphenylgermylene (2-methyl-4-phenylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(35) dichloro {1,1′-germacyclobutenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(36) Dichloro {1,1′-germacyclopropenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(37) dichloro {1,1′-germafluorenyl (2,4,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium,
(38) Dichloro [dimethylsilylene {2-methyl-4- (2-methylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(39) Dichloro [dimethylsilylene {2-methyl-4- (cyclopropylmethyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(40) Dichloro [dimethylsilylene {3- (2-methylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,

(41) Dichloro [dimethylsilylene {2-methyl-4- (2,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(42) Dichloro [dimethylsilylene {2-methyl-4- (cyclohexylmethyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(43) Dichloro [dimethylsilylene {2-methyl-4- (1,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(44) Dichloro [dimethylsilylene {3- (1-cyclopropylethyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(45) Dichloro [dimethylsilylene {3- (1,2-dimethylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(46) Dichloro [dimethylsilylene {2-methyl-4- (1,2,2-trimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(47) Dichloro [dimethylsilylene {3- (1-cyclohexylethyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(48) Dichloro [dimethylsilylene {2-methyl-4- (1-i-propylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(49) Dichloro [dimethylsilylene {2-methyl-4- (1-cyclopropylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(50) dichloro [dimethylsilylene {3- (1-ethyl-2-methylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(51) Dichloro [dimethylsilylene {2-methyl-4- (1-t-butylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(52) Dichloro [dimethylsilylene {2-methyl-4- (1-cyclohexylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(53) Dichloro [dimethylsilylene {3- (1-i-propylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(54) Dichloro [dimethylsilylene {3- (1-cyclopropylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(55) Dichloro [dimethylsilylene {3- (1-s-butylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azuler)] hafnium,
(56) Dichloro [dimethylsilylene {3- (1-t-butylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azuler)] hafnium,
(57) Dichloro [dimethylsilylene {3- (1-cyclohexylbutyl) -5-methylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(58) Dichloro [dimethylsilylene {2-ethyl-4- (2-methylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(59) Dichloro [dimethylsilylene {2-ethyl-4- (cyclopropylmethyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(60) Dichloro [dimethylsilylene {3- (2-methylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,

(61) Dichloro [dimethylsilylene {2-ethyl-4- (2,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(62) Dichloro [dimethylsilylene {2-ethyl-4- (cyclohexylmethyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(63) Dichloro [dimethylsilylene {2-ethyl-4- (1,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(64) Dichloro [dimethylsilylene {2-ethyl-4- (1-cyclopropylethyl) -methyl) -cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(65) Dichloro [dimethylsilylene {3- (1,2-dimethylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(66) Dichloro [dimethylsilylene {2-ethyl-4- (1,2,2-trimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(67) Dichloro [dimethylsilylene {2-ethyl-4- (1-cyclohexylethyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(68) Dichloro [dimethylsilylene {2-ethyl-4- (1-i-propylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(69) Dichloro [dimethylsilylene {2-ethyl-4- (1-cyclopropylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(70) dichloro [dimethylsilylene {3- (1-ethyl-2-methylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(71) Dichloro [dimethylsilylene {2-ethyl-4- (1-t-butylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(72) Dichloro [dimethylsilylene {2-ethyl-4- (1-cyclohexylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(73) Dichloro [dimethylsilylene {3- (1-i-propylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(74) Dichloro [dimethylsilylene {3- (1-cyclopropylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(75) Dichloro [dimethylsilylene {3- (1-s-butylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(76) Dichloro [dimethylsilylene {3- (1-t-butylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(77) Dichloro [dimethylsilylene {3- (1-cyclohexylbutyl) -5-ethylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(78) Dichloro [dimethylsilylene {2-n-propyl-4- (2-methylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(79) Dichloro [dimethylsilylene {3- (cyclopropylmethyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(80) Dichloro [dimethylsilylene {3- (2-methylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,

(81) Dichloro [dimethylsilylene {2-n-propyl-4- (2,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(82) Dichloro [dimethylsilylene {3- (cyclohexylmethyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(83) Dichloro [dimethylsilylene {2-n-propyl-4- (1,2-dimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(84) Dichloro [dimethylsilylene {3- (1-cyclopropylethyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(85) Dichloro [dimethylsilylene {3- (1,2-dimethylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(86) Dichloro [dimethylsilylene {2-n-propyl-4- (1,2,2-trimethylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(87) Dichloro [dimethylsilylene {3- (1-cyclohexylethyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(88) Dichloro [dimethylsilylene {2-n-propyl-4- (1-i-propylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(89) Dichloro [dimethylsilylene {2-n-propyl-4- (1-cyclopropylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(90) Dichloro [dimethylsilylene {3- (1-ethyl-2-methylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(91) Dichloro [dimethylsilylene {2-n-propyl-4- (1-t-butylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(92) Dichloro [dimethylsilylene {2-n-propyl-4- (1-cyclohexylpropyl) cyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(93) Dichloro [dimethylsilylene {3- (1-i-propylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(94) Dichloro [dimethylsilylene {3- (1-cyclopropylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(95) Dichloro [dimethylsilylene {3- (1-s-butylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(96) Dichloro [dimethylsilylene {3- (1-t-butylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium,
(97) Dichloro [dimethylsilylene {3- (1-cyclohexylbutyl) -5-n-propylcyclopentadienyl} (2-methyl-4-phenyl-4H-azurenyl)] hafnium, and the like.
In addition, when the component [A-2] having the structure described above is selected, a component different from the structure of the component [A-1] is selected.

Moreover, as a non-limiting preferable example of the component [A-2], when E ²¹ and E ²² are a cyclopentadienyl group and a fluorenyl group, the following structures can be exemplified.

In the general formula (a7), R ⁷² is selected from a silyl group having a hydrocarbon group having 1 to 20 carbon atoms or a hydrocarbon group having 1 to 20 carbon atoms, preferably a methyl group, an ethyl group, an isopropyl group, t -A butyl group and a trimethylsilyl group. R ⁷¹ , R ⁷³ , R ⁷⁴ , R ⁷⁵ , R ⁷⁶ , R ⁷⁷ and R ⁷⁸ are selected from a hydrogen atom, a hydrocarbon group having 1 to 20 carbon atoms or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms, Each may be the same or different, and adjacent substituents from R ^{75 to} R ⁷⁸ may be bonded to each other to form a ring.
Moreover, said ^X71 and ^Y71 are auxiliary ligands, and react with component [B] as a cocatalyst to produce an active metallocene having olefin polymerization ability. In order to achieve this purpose, X ⁷¹ and Y ⁷¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, an alkoxy group having 1 to 20 carbon atoms, or 1 to 20 carbon atoms. An alkylamide group, a trifluoromethanesulfonic acid group, a phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms.

In addition, the Q ⁷¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms that bridges two conjugated five-membered ligands via carbon having 1 or 2 carbon atoms, which bonds two five-membered rings. , Either a silylene group or a germylene group optionally having a hydrocarbon group having 1 to 20 carbon atoms is shown. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of the Q ^71, methylene, methylmethylene, dimethylmethylene, 1,2-ethylene, alkylene group and the like; silylene group; arylalkylene groups such as diphenylmethylene methylsilylene, dimethylsilylene, diethyl silylene, di ( n-propyl) silylene, di (i-propyl) silylene, alkylsilylene groups such as di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; tetra An alkyl oligosilylene group such as methyldisilylene; a germylene group; an alkylgermylene group in which the silicon of the above-mentioned divalent hydrocarbon group having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) germylene Group; arylgermylene group And so on.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.
Further, M ⁷¹ is zirconium or hafnium, preferably hafnium.

Among the compounds represented by the general formula (a7),
(1) dichlorodimethylmethylene (3-i-propylcyclopentadienyl) fluorenyl) zirconium,
(2) dichlorodimethylmethylene (3-tert-butylcyclopentadienyl) fluorenyl) zirconium,
(3) dichlorodimethylmethylene (3-trimethylsilylcyclopentadienyl) fluorenyl) zirconium,
(4) dichlorodimethylmethylene (3- (t-butyldimethylsilyl) cyclopentadienyl) fluorenyl) zirconium,
(5) dichlorodimethylmethylene (3-i-propyl-5-methylcyclopentadienyl) fluorenyl) zirconium,
(6) dichlorodimethylmethylene (3-tert-butyl-5-methylcyclopentadienyl) fluorenyl) zirconium,
(7) dichlorodimethylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) fluorenyl) zirconium,
(8) dichlorodimethylmethylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) fluorenyl) zirconium,
(9) dichlorodimethylmethylene (3-i-propyl-5-ethylcyclopentadienyl) fluorenyl) zirconium,
(10) dichlorodimethylmethylene (3-t-butyl-5-ethylcyclopentadienyl) fluorenyl) zirconium,
(11) dichlorodimethylmethylene (3-trimethylsilyl-5-ethylcyclopentadienyl) fluorenyl) zirconium,
(12) dichlorodimethylmethylene (3- (t-butyldimethylsilyl) -5-ethylcyclopentadienyl) fluorenyl) zirconium,
(13) dichlorodimethylmethylene (3-i-propyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(14) dichlorodimethylmethylene (3-tert-butyl-5-methylcyclopentadienyl) (3,6-ditert-butylfluorenyl) zirconium,
(15) dichlorodimethylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(16) dichlorodimethylmethylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(17) dichlorodimethylmethylene (3-i-propyl-5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium,
(18) dichlorodimethylmethylene (3-t-butyl-5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium,
(19) dichlorodimethylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium,
(20) dichlorodimethylmethylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) (2,7-di-t-butylfluorenyl) zirconium,

(21) dichlorodimethylmethylene (3-tert-butyl-5-methylcyclopentadienyl) (dibenzo [b, h] fluorenyl) zirconium,
(22) dichlorodimethylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) (dibenzo [b, h] fluorenyl) zirconium,
(23) Dichlorodimethylmethylene (3-t-butyl-5-methylcyclopentadienyl) (1,1,4,4,7,7,10,10-octamethyl-1,2,3,4,7, 8,9,10-octahydrodibenzofluorenyl) zirconium,
(24) Dichlorodimethylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) (1,1,4,4,7,7,10,10-octamethyl-1,2,3,4,7,8, 9,10-octahydrodibenzo [b, h] fluorenyl) zirconium,
(25) dichlorodiphenylmethylene (3-i-propyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(26) dichlorodiphenylmethylene (3-t-butyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(27) dichlorodiphenylmethylene (3-trimethylsilyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(28) dichlorodiphenylmethylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(29) dichlorodimethylsilylene (3-i-propyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(30) dichlorodimethylsilylene (3-t-butyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(31) dichlorodimethylsilylene (3-trimethylsilyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(32) dichlorodimethylsilylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(33) dichlorodiphenylsilylene (3-i-propyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(34) dichlorodiphenylsilylene (3-t-butyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(35) dichlorodiphenylsilylene (3-trimethylsilyl-5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium,
(36) Dichlorodiphenylsilylene (3- (t-butyldimethylsilyl) -5-methylcyclopentadienyl) (3,6-di-t-butylfluorenyl) zirconium.

Moreover, as a non-limiting preferable example of the component [A-2], when E ²¹ and E ²² are an indenyl group and an azulenyl group, the following structures can be exemplified.

In the general formula (a8), R ⁸¹ and R ⁸² are each independently a hydrocarbon group having 1 to 6 carbon atoms, preferably an alkyl group, more preferably an alkyl group having 1 to 4 carbon atoms. It is. Specific examples include methyl, ethyl, n-propyl, i-propyl, n-butyl, i-butyl, sec-butyl, n-pentyl, i-pentyl, n-hexyl, and preferably methyl. , Ethyl, n-propyl.
R ⁸³ and R ⁸⁴ each independently contain halogen, silicon, or a plurality of heteroelements selected from these, having 6 to 30 carbon atoms, preferably 6 to 24 carbon atoms. Of the aryl group. Such an aryl group is a phenyl group, a biphenylyl group, or a naphthyl group which may have a substituent. Preferable examples include phenyl, 3-chlorophenyl, 4-chlorophenyl, 3-fluorophenyl, 4-fluorophenyl, 4-methylphenyl, 4-i-propylphenyl, 4-t-butylphenyl, 4-trimethylsilylphenyl, 4 -(2-fluoro-4-biphenylyl), 4- (2-chloro-4-biphenylyl), 1-naphthyl, 2-naphthyl, 4-chloro-2-naphthyl, 3-methyl-4-trimethylsilylphenyl, 3, Examples include 5-dimethyl-4-t-butylphenyl, 3,5-dimethyl-4-trimethylsilylphenyl, 3,5-dichloro-4-trimethylsilylphenyl, and the like.

Moreover, said ^X81 and ^Y81 are auxiliary ligands, and react with component [B] as a cocatalyst to produce an active metallocene having olefin polymerization ability. Therefore, as long as this object is achieved, X ⁵¹ and Y ⁵¹ are not limited in the type of ligand, and are independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, An alkoxy group having 1 to 20 carbon atoms, an alkylamide group having 1 to 20 carbon atoms, a trifluoromethanesulfonic acid group, a phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or a silicon-containing hydrocarbon group having 1 to 20 carbon atoms. Show.
Q ⁸¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms that bonds two conjugated five-membered ring ligands through carbon having 1 or 2 carbon atoms, which bonds two five-membered rings, It shows either a silylene group or a germylene group which may have a hydrocarbon group having 1 to 20 carbon atoms. When two hydrocarbon groups are present on the above-mentioned silylene group or germylene group, they may be bonded to each other to form a ring structure.
Specific examples of Q ⁸¹ include alkylene groups such as methylene, methylmethylene, dimethylmethylene and 1,2-ethylene; arylalkylene groups such as diphenylmethylene; silylene groups; methylsilylene, dimethylsilylene, diethylsilylene, di Alkylsilylene groups such as (n-propyl) silylene, di (i-propyl) silylene, di (cyclohexyl) silylene, (alkyl) (aryl) silylene groups such as methyl (phenyl) silylene; arylsilylene groups such as diphenylsilylene; Alkyl oligosilylene groups such as tetramethyldisilene; germylene groups; alkylgermylene groups in which silicon in the above-mentioned divalent hydrocarbon groups having 1 to 20 carbon atoms is replaced with germanium; (alkyl) (aryl) Germylene group; arylgermylene Examples include groups.
In these, the silylene group which has a C1-C20 hydrocarbon group, or the germylene group which has a C1-C20 hydrocarbon group is preferable, and an alkylsilylene group and an alkylgermylene group are especially preferable.
Further, M ⁸¹ is zirconium or hafnium, preferably hafnium.

Among the compounds represented by the general formula (a8),
(1) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4-phenyl-4H-1-azurenyl)] hafnium,
(2) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4-phenyl-4H-1-azurenyl)] hafnium,
(3) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (4-chlorophenyl) -4H-1-azurenyl)] hafnium,
(4) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (4-chlorophenyl) -4H-1-azurenyl)] hafnium,
(5) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (4-fluorophenyl) -4H-1-azurenyl)] hafnium,
(6) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (4-fluorophenyl) -4H-1-azurenyl)] hafnium,
(7) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (4-t-butylphenyl) -4H-1-azulenyl)] hafnium,
(8) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (4-t-butylphenyl) -4H-1-azurenyl)] hafnium,
(9) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (4-trimethylsilylphenyl) -4H-1-azurenyl)] hafnium,
(10) Dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (4-trimethylsilylphenyl) -4H-1-azurenyl)] hafnium,
(11) dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (1-naphthyl) -4H-1-azurenyl)] hafnium,
(12) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (1-naphthyl) -4H-1-azurenyl)] hafnium,
(13) Dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4- (2-naphthyl) -4H-1-azurenyl)] hafnium,
(14) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-methyl-4- (2-naphthyl) -4H-1-azurenyl)] hafnium,
(15) Dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-ethyl-4-phenyl-4H-1-azurenyl)] hafnium,
(16) Dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-ethyl-4-phenyl-4H-1-azurenyl)] hafnium,
(17) Dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-ethyl-4- (4-chlorophenyl) -4H-1-azurenyl)] hafnium,
(18) dichloro [dimethylsilylene (2-ethyl-4-phenyl-1-indenyl) (2-ethyl-4- (4-chlorophenyl) -4H-1-azurenyl)] hafnium,
(19) Dichloro [dimethylsilylene (2-methyl-4-phenyl-1-indenyl) (2-methyl-4-phenyl-4H-5,6,7,8-tetrahydro-1-azurenyl)] hafnium,
(20) Dichloro [dimethylsilylene (2-ethyl-1-indenyl) (2-methyl-4-phenyl-4H-5,6,7,8-tetrahydro-1-azulenyl)] hafnium.

(3) Component [B]
As the component [B], an aluminum oxy compound [B-1], an ionic compound that can be converted into a cation by reacting with the above transition metal compounds [A-1] and [A-2], or a Lewis acid [ At least one selected from the group consisting of B-2], solid acid fine particles [B-3], and ion-exchange layered silicate [B-4] is used.

(3-1) Component [B-1]
Specific examples of the aluminum oxy compound [B-1] include compounds represented by the following general formula (9), (10) or (11).

In each of the above general formulas, R ⁹¹ , R ¹⁰¹ and R ¹¹¹ represent a hydrogen atom or a hydrocarbon residue, preferably a hydrocarbon residue having 1 to 10 carbon atoms, particularly preferably 1 to 6 carbon atoms. A plurality of R ⁹¹ , R ¹⁰¹ and R ¹¹¹ may be the same or different. P represents an integer of 0 to 40, preferably 2 to 30.
The compounds represented by the general formulas (9) and (10) are also called alumoxanes. Among these, methylalumoxane or methylisobutylalumoxane is preferable.
The above-mentioned alumoxane can be used in combination within a group and between groups. And said alumoxane can be prepared on well-known various conditions.
The compound represented by the general formula (11) is 10: 1 to 1 of one type of trialkylaluminum or two or more types of trialkylaluminum and an alkylboronic acid represented by the following general formula (12). : 1 (molar ratio) reaction.
In General Formulas (11) and (12), R ¹¹² and R ¹²¹ represent a hydrocarbon residue or a halogenated hydrocarbon group having 1 to 10 carbon atoms, preferably 1 to 6 carbon atoms.

  Component [B-1] is used by being supported on a particulate carrier. The fine particle carrier will be described later.

(3-2) Component [B-2]
Component [B-2] is an ionic compound or Lewis acid that can be converted to a cation by reacting with the transition metal compound [A] described above.
Specifically, the ionic compound includes a cation such as a carbonium cation or an ammonium cation, and an organic boron compound such as triphenylboron, tris (3,5-difluorophenyl) boron, or tris (pentafluorophenyl) boron. And a complex with a cation.
Examples of the Lewis acid that can convert the component [A] into a cation include various organoboron compounds such as tris (pentafluorophenyl) boron. Alternatively, metal halogen compounds such as aluminum chloride and magnesium chloride are exemplified.
In addition, a certain thing of said Lewis acid can also be grasped | ascertained as an ionic compound which can react with component [A] and can convert component [A] into a cation. Therefore, the compounds belonging to both the Lewis acid and the ionic compound belong to either one.
Component [B-2] is used by being supported on a particulate carrier. The fine particle carrier will be described later.

(3-3) Component [B-3]
Examples of the solid acid fine particles [B-3] include solid acids such as alumina and silica-alumina.
Here, the particulate carrier in [B-1] and [B-2] described above will be described.
In the present invention, the elemental composition and the compound composition of the particulate carrier are not particularly limited. For example, a particulate carrier made of an inorganic or organic compound can be exemplified. Examples of the inorganic carrier include silica, alumina, silica / alumina magnesium chloride, activated carbon, inorganic silicate, and the like. Alternatively, a mixture thereof may be used.
Examples of the organic carrier include polymers of α-olefins having 2 to 14 carbon atoms such as ethylene, propylene, 1-butene and 4-methyl-1-pentene, and aromatic unsaturated carbonization such as styrene and divinylbenzene. Examples thereof include a porous polymer fine particle carrier made of a polymer of hydrogen. Alternatively, a mixture thereof may be used.
These fine particle carriers usually have an average particle diameter of 1 μm to 5 mm, preferably 5 μm to 1 mm, more preferably 10 μm to 200 μm.

(3-4) Component [B-4]
Component [B-4] is an ion-exchange layered silicate (hereinafter simply referred to as silicate).
In the present invention, the silicate used as a raw material is a silicate compound having a crystal structure in which the surfaces constituted by ionic bonds and the like are stacked in parallel with each other and having exchangeable ions. Say. Most silicates are naturally produced mainly as a main component of clay minerals, and therefore often contain impurities (quartz, cristobalite, etc.) other than ion-exchangeable layered silicates. But you can. Specific examples of the silicate include the following layered silicates described in Haruo Shiramizu “Clay Mineralogy” Asakura Shoten (1995).
That is, montmorillonite, sauconite, beidellite, nontronite, saponite, hectorite, stemite and other smectites, vermiculite and other vermiculites, mica, illite, sericite and sea chlorite and other mica, attapulgite, sepiolite and palygorskite , Bentonite, pyrophyllite, talc, chlorite group, etc.

The silicate used as a raw material in the present invention is preferably a silicate in which the main component silicate has a 2: 1 type structure, more preferably a smectite group, and particularly preferably montmorillonite. The type of interlayer cation is not particularly limited, but a silicate containing an alkali metal or an alkaline earth metal as a main component of the interlayer cation is preferable from the viewpoint of being relatively easy and inexpensive to obtain as an industrial raw material.
Although the silicate used by this invention can be used as it is, without performing a process especially, it is preferable to give a chemical process. Here, the chemical treatment may be any of a surface treatment that removes impurities adhering to the surface and a treatment that affects the structure of the clay. Specific examples of the chemical treatment in the present invention include (a) acid treatment, (b) salt treatment, (c) alkali treatment, (d) organic matter treatment, and the like described below.

(A) Acid treatment In addition to removing impurities on the surface, the acid treatment can elute some or all of cations such as Al, Fe, Mg, etc. having a crystal structure.
The acid used in the acid treatment is preferably selected from hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, acetic acid and oxalic acid. Two or more salts and acids may be used in the treatment. The treatment conditions with salts and acids are not particularly limited, but usually the salt and acid concentrations are selected from 0.1 to 50% by weight, the treatment temperature is from room temperature to boiling point, and the treatment time is from 5 minutes to 24 hours. Then, it is preferable to carry out under the condition that at least a part of the substance constituting at least one compound selected from the group consisting of ion-exchanged layered silicate is eluted. In addition, salts and acids are generally used in an aqueous solution.

(B) Salt treatment In the present invention, 40% or more, preferably 60% or more, of the exchangeable Group 1 metal cation contained in the ion-exchangeable layered silicate before treatment with salts is described below. It is preferable to exchange ions with cations dissociated from the salts shown.

The salt used in the salt treatment for the purpose of ion exchange is a group consisting of a cation containing at least one atom selected from the group consisting of group 1 to 14 atoms, a halogen atom, an inorganic acid, and an organic acid. A compound comprising at least one anion selected from the group consisting of at least one anion selected from the group consisting of 2 to 14 atoms, and Cl, Br, I, F, PO. ₄ , SO ₄ , NO ₃ , CO ₃ , C ₂ O ₄ , ClO ₄ , OOCCH ₃ , CH ₃ COCHCOCH ₃ , OCl ₂ , O (NO ₃ ) ₂ , O (ClO ₄ ) ₂ , O (SO ₄ ), At least one anion selected from the group consisting of OH, O ₂ Cl ₂ , OCl ₃ , OOCH, OOCCH ₂ CH ₃ , C ₂ H ₄ O ₄ and C ₅ H ₅ O ₇ Is a compound consisting of

_{Specifically, LiF, LiCl, LiBr, LiI} , Li 2 SO 4, Li (CH 3 COO), LiCO 3, Li (C 6 H 5 O 7), LiCHO 2, LiC 2 O 4, LiClO 4, Li ₃ PO ₄ , CaCl ₂ , CaSO ₄ , CaC ₂ O ₄ , Ca (NO ₃ ) ₂ , Ca ₃ (C ₆ H ₅ O ₇ ) ₂ , MgCl ₂ , MgBr ₂ , MgSO ₄ , Mg (PO ₄ ) ₂ , Mg (ClO ₄ ) ₂ , MgC ₂ O ₄ , Mg (NO ₃ ) ₂ , Mg (OOCCH ₃ ) ₂ , MgC ₄ H ₄ O ₄ , Ti (OOCCH ₃ ) ₄ , Ti (CO ₃ ) ₂ , Ti (NO ₃ ) ₄ , Ti (SO ₄ ) ₂ , TiF ₄ , TiCl ₄ , Zr (OOCCH ₃ ) ₄ , Zr (CO ₃ ) ₂ , Zr (NO ₃ ) ₄ , Zr (SO ₄ ) ₂ , Zr F ₄ , ZrCl ₄ , ZrOCl ₂ , ZrO (NO ₃ ) ₂ , ZrO (ClO ₄ ) ₂ , ZrO (SO ₄ ), HF (OOCCH ₃ ) ₄ , HF (CO ₃ ) ₂ , HF (NO ₃ ) ₄ , _{HF (SO 4) 2, HFOCl} 2, HFF 4, HFCl 4, V (CH 3 COCHCOCH 3) 3, VOSO 4, VOCl 3, VCl 3, VCl 4, VBr 3 , etc. _{and, Cr (CH 3 COCHCOCH 3)} 3 Cr (OOCCH ₃ ) ₂ OH, Cr (NO ₃ ) ₃ , Cr (ClO ₄ ) ₃ , CrPO ₄ , Cr ₂ (SO ₄ ) ₃ , CrO ₂ Cl ₂ , CrF ₃ , CrCl ₃ , CrBr ₃ , CrI _{3 , Mn (OOCCH 3) 2,} Mn (CH 3 COCHCOCH 3) 2, MnCO 3, Mn (NO 3) 2, MnO, Mn _{ClO 4) 2, MnF 2,} MnCl 2, Fe (OOCCH 3) 2, Fe (CH 3 COCHCOCH 3) 3, FeCO 3, Fe (NO 3) 3, Fe (ClO 4) 3, FePO 4, FeSO 4, Fe ₂ (SO ₄ ) ₃ , FeF ₃ , FeCl ₃ , FeC ₆ H ₅ O ₇ , Co (OOCCH ₃ ) ₂ , Co (CH ₃ COCHCOCH ₃ ) ₃ , CoCO ₃ , Co (NO ₃ ) ₂ , CoC ₂ O ₄ , Co (ClO ₄ ) ₂ , Co ₃ (PO ₄ ) ₂ , CoSO ₄ , CoF ₂ , CoCl ₂ , NiCO ₃ , Ni (NO ₃ ) ₂ , NiC ₂ O ₄ , Ni (ClO ₄ ) ₂ , NiSO ₄ , NiCl ₂ , NiBr _2, etc., Zn (OOCCH ₃ ) ₂ , Zn (CH ₃ COCHCOCH ₃ ) ₂ , ZnCO ₃ , Z n (NO ₃ ) ₂ , Zn (ClO ₄ ) ₂ , Zn ₃ (PO ₄ ) ₂ , ZnSO ₄ , ZnF ₂ , ZnCl ₂ , AlF ₃ , AlCl ₃ , AlBr ₃ , AlI ₃ , Al ₂ (SO ₄ ) ₃ Al ₂ (C ₂ O ₄ ) ₃ , Al (CH ₃ COCHCOCH ₃ ) ₃ , Al (NO ₃ ) ₃ , AlPO ₄ , GeCl ₄ , GeBr ₄ , GeI _{4 and the} like.

(C) Alkali treatment Examples of the treating agent used in the alkali treatment include LiOH, NaOH, KOH, Mg (OH) ₂ , Ca (OH) ₂ , Sr (OH) ₂ , Ba (OH) ₂ .

(D) Organic matter treatment Examples of the organic matter used for the organic matter treatment include trimethylammonium, triethylammonium, N, N-dimethylanilinium, triphenylphosphonium, and the like.
Further, examples of the anion constituting the organic treatment agent include hexafluorophosphate, tetrafluoroborate, and tetraphenylborate other than the anion exemplified as the anion constituting the salt treatment agent. However, it is not limited to these.

These ion-exchange layered silicates usually contain adsorbed water and interlayer water. In the present invention, it is preferable to remove these adsorbed water and interlayer water and use them as component [B].
The heat treatment method of the adsorbed layered silicate adsorbed water and interlayer water is not particularly limited, but it is desirable to select conditions so that the interlayer water does not remain and structural destruction does not occur. The heating time is 0.5 hour or longer, preferably 1 hour or longer. At that time, the water content of the component b after removal is 3% by weight or less, preferably 1 when the water content is 0% by weight when dehydrated for 2 hours under the conditions of a temperature of 200 ° C. and a pressure of 1 mmHg. It is preferable that it is below wt%.

As described above, in the present invention, as the component [B], an ion-exchange layered silicate having a water content of 3% by weight or less obtained by performing a salt treatment and / or an acid treatment is particularly preferable. It is.
The ion-exchange layered silicate can be treated with the component [C] described later before being used as a catalyst or as a catalyst, which is preferable. Although there is no restriction | limiting in the usage-amount of component [C] with respect to 1g of ion-exchange layered silicate, Usually, 20 mmol or less, Preferably it is 0.5 mmol or more and 10 mmol or less. There is no limitation on the treatment temperature and time, the treatment temperature is usually 0 ° C. or more and 70 ° C. or less, and the treatment time is 10 minutes or more and 3 hours or less. It is also possible and preferable to wash after the treatment. As the solvent, the same hydrocarbon solvent as that used in the preliminary polymerization and slurry polymerization described later is used.

The component [B] is preferably spherical particles having an average particle diameter of 5 μm or more. If the particle shape is spherical, a natural product or a commercially available product may be used as it is, or a particle whose particle shape and particle size are controlled by granulation, sizing, fractionation or the like may be used.
Examples of the granulation method used here include agitation granulation method and spray granulation method, but commercially available products can also be used.
Moreover, you may use organic substance, an inorganic solvent, inorganic salt, and various binders in the case of granulation.

  The spherical particles obtained as described above desirably have a compressive fracture strength of 0.2 MPa or more, particularly preferably 0.5 MPa or more, in order to suppress crushing and generation of fine powder in the polymerization step. In the case of such particle strength, the effect of improving the particle properties is effectively exhibited especially when prepolymerization is performed.

Among the above-mentioned component [B], [B-4] ion-exchange layered silicate is particularly preferable.
In the propylene polymerization catalyst according to the present invention, [B-1] an aluminum oxy compound, [B-2] an ionic compound capable of reacting with component [A] to convert component [A] into a cation, or Lewis The acid, [B-3] solid acid fine particles, or [B-4] ion-exchange layered silicate fine particles are each used alone as the component [B], and these four components can be combined as appropriate, Can be used.

(4) Component [C]
As the component [C], an organoaluminum compound is used. In the present invention, the following general formula:
AlR ⁷¹ _q Z _3-q ... General formula (13)
An organoaluminum compound represented by the formula is preferred.
In the present invention, it goes without saying that the compounds represented by this formula can be used singly or in combination of two or more. In this formula, R ⁷¹ represents a hydrocarbon group having 1 to 20 carbon atoms, and Z represents a halogen atom, a hydrogen atom, an alkoxy group, or an amino group. q is a number greater than 0 and up to 3. R ⁷¹ is preferably an alkyl group, and Z is a chlorine atom when it is a halogen atom, a C 1-8 alkoxy group when it is an alkoxy group, and a carbon atom number 1 when it is an amino group. An amino group of ˜8 is preferred.

Specific examples of preferred organoaluminum compounds include trimethylaluminum, triethylaluminum, trinormalpropylaluminum, trinormalbutylaluminum, triisobutylaluminum, trinormalhexylaluminum, trinormaloctylaluminum, trinormaldecylaluminum, diethylaluminum chloride, diethyl Examples include aluminum sesquichloride, diethylaluminum hydride, diethylaluminum ethoxide, diethylaluminum dimethylamide, diisobutylaluminum hydride, diisobutylaluminum chloride and the like.
Of these, trialkylaluminum and dialkylaluminum hydrides with q = 3 are preferred. More ^preferably trialkylaluminum ^{R 71} is 1 to 8 carbon atoms.

2. Method for Producing Olefin Polymerization Catalyst The method for producing an olefin polymerization catalyst of the present invention is characterized by sequentially performing the following steps [I] to [III].
Step [I]: A step of producing a contact product (1) by bringing component [A-1] into contact with components [B] and [C].
Step [II]: a step of washing the contact product (1) obtained in step [I] with an inert hydrocarbon solvent so that the washing rate is 1/10 or less to produce a washed product. .
Step [III]: A step of producing a contact product (2) by bringing the component [A-2] into contact with the washed product obtained in Step [II].
However, the molar ratio [A-1] / [A-2] of [A-1] to component [A-2] is 1.0 to 99.0.

(1) Process [I]
Step [I] is a step of producing contact product (1) by bringing component [A-1] into contact with components [B] and [C].
It can form by making said component [A-1] and component [B] contact simultaneously or continuously, or once or several times.
In addition, when the component [A-1] and the component [B] are contacted, the component [C] can be contacted simultaneously or continuously, or once or a plurality of times.
These contact orders can be combined in any desired manner, but particularly preferable ones for each component are as follows.
(I) Before contacting the component [A-1] and the component [B], the component [A-1], the component [B], or both the component [A-1] and the component [B] Contacting component [C], or (ii) contacting component [C-1] simultaneously with component [A-1] and component [B], or (iii) component [A] -1] and component [B] can be contacted, and then component [C] can be contacted, but preferably (i) before contacting component [A-1] and component [B]. , Component [C] is brought into contact with either.
At this time, the amount of component [C] used is preferably in contact with component [A-1] in the range of [C] / [A-1] = 0.3 to 100 (molar ratio). .

Component [C] reacts with component [A-1] in the presence of component [B] to form an active species. Specifically, when alkylaluminum is used as component [C], when the auxiliary ligand of component [A-1] is other than an alkyl group such as halogen, the auxiliary ligand is substituted with an alkyl group. By doing so, active species are generated.
Therefore, if the amount of the component [C] used is too small, this substitution reaction becomes insufficient and the activity may be lowered. Therefore, the amount of component [C] used is preferably 0.3 or more, more preferably 0.6 or more, and still more preferably 1.0 or more, in molar ratio with respect to component [A-1]. .
In addition, when the component [A-1] has a substituent containing a heteroatom at the 2-position of the indenyl ring, the component [C] is present in the vicinity of the heteroatom so that the component [A-1] The present inventors consider that, when brought into contact with [A-2], it is possible to prevent this heteroatom from acting on the component [A-2] and reducing the activity. Therefore, the amount of component [C] used is preferably 2.0 or more, more preferably 3.0 or more, and still more preferably 4.0 or more, in molar ratio with respect to component [A-1]. .
On the other hand, although the mechanism or the mechanism is not necessarily clear, the component [C] reacts with the component [A-1] to cause a side reaction that the component [A-1] is decomposed or poisoned. They are thinking. Therefore, the amount of component [C] used is preferably 100 or less, more preferably 50 or less, and even more preferably 10 or less, in molar ratio with respect to component [A-1].

  The contacting of each component is usually performed in an aliphatic hydrocarbon or an aromatic hydrocarbon solvent. Although the contact temperature is not particularly limited, it is carried out between −20 ° C. and 150 ° C., but it is preferably carried out between 0 ° C. and 60 ° C., more preferably 10 ° C. Between 30 ° C is preferred.

(2) Process [II]
Step [II] is a step of washing the contact product (1) obtained in step [I] with an inert hydrocarbon solvent to produce a washed product.
That is, after contacting each component in the step [I], washing with an aliphatic hydrocarbon or aromatic hydrocarbon solvent does not carry the component [B] in the solvent in the step [I]. This is a step of removing the remaining component [A-1] from the system.
If the component [A-1] and the component [A-2] are simultaneously present in the solvent, the mechanism of action is not necessarily clear at the present time, but they interact with each other and reduce poisoning or activity. The present inventors think.
Therefore, it is desirable to sufficiently reduce the amount of the component [A-1] liberated in the solvent by washing, and for that purpose, it is necessary to carry out washing so that the washing rate is 1/10 or less. is there. On the other hand, since excessive cleaning may cause the supported component [A-1] to be extracted, a cleaning rate of 1/1000 or more is necessary.
In addition, when Component [A-1] has a substituent containing a hetero atom at the 2-position of the indenyl ring as defined in General Formula (a1), a large amount of Component [A-1] is present in the solvent. If the contact step with the next component [A-2] is performed while remaining in the structure, the hetero atom on the component [A-1] acts on the component [A-2], and the component [A-2] We believe that some will be poisoned or reduce activity.
Therefore, it is desirable to sufficiently reduce the amount of the component [A-1] liberated in the solvent by washing, and for that purpose, washing is performed in the range of 1/10 to 1/1000 as the washing rate. More preferably, the cleaning is preferably performed in the range of 1/50 to 1/1000.

Here, the washing rate represents the degree of washing at the time of washing and is the residual liquid rate, that is, the amount of liquid remaining after washing is the total amount of liquid when the washing solvent is added. When the cleaning is performed a plurality of times, a value obtained by multiplying the respective cleaning rates is obtained.
For example, in the case of decantation, the amount of each component contained in the supernatant is defined as a total amount 1, and the amount of the components originally present in the supernatant after the washing is included in the following amount. It is obtained by a calculation formula. In the decantation washing, one cycle (one time) is from the addition of the solvent to the extraction of the supernatant.
W ₁ = (V ₀ + P ₁ −d ₁ ) / (V ₀ + P ₁ )
W ₂ = (V ₁ + P ₂ −d ₂ ) / (V ₁ + P ₂ )
_{W n = (V n-1} + P n -d n) / (V n-1 + P n)
Cleaning rate = W ₁ × W ₂ .. × W _n
However, the symbols have the following meanings.
W _n : Cleaning rate of the nth time (0 time indicates before cleaning, and W ₀ = 1)
V _n-1 : (n-1) Solution amount after the n-th washing d _n : Amount of solution extracted at the n-th washing P _n : Amount of additional inert hydrocarbon solvent at the n-th washing

The solvent used for washing in the process is an inert hydrocarbon solvent, preferably a saturated aliphatic or aromatic hydrocarbon such as hexane, heptane, pentane, cyclohexane, benzene, toluene, or a mixture thereof. it can.
Moreover, the temperature at the time of washing | cleaning can be 0 degreeC or more and 100 degrees C or less, Preferably it is 10 degreeC or more and 80 degrees C or less.
Furthermore, the time for stirring in the washing step can be from 5 minutes to 30 minutes. Moreover, after washing, it is preferable that the settling time is 5 minutes to 1 hour, preferably 10 minutes to 30 minutes.

(3) Process [III]
Step [III] is a step for producing a contact product (2) by bringing component [A-2] into contact with the washed product obtained in step [II].
In other words, the component [A-2] is activated and loaded on the component [B] by adding the component [A-2] to the washed product generated in the step [II].
Also in this case, component [C] reacts with component [A-2] in the presence of component [B] to form an active species. Specifically, when alkylaluminum is used as component [C], an active species is generated by substituting the auxiliary ligand of component [A-2] with an alkyl group.
Therefore, when there is too little quantity of component [C] to use, this activation will become inadequate and activity will fall. Therefore, the amount of the component [C] used is preferably 0.3 or more, more preferably 0.6 or more, and still more preferably 1.0 or more with respect to the component [A-2]. is there.
On the other hand, although the mechanism or mechanism of the component [C] is not necessarily clear, the present inventors consider that it causes a side reaction of reacting with the component [A-2] to decompose or poison. Therefore, the amount of component [C] used is preferably 10 or less, more preferably 5 or less, in molar ratio to component [A-2].
Here, the amount of the component [C] in the step [III] is the amount obtained by multiplying the amount of the component [C] added in the step [I] by the washing rate and the component newly added in the step [III]. The amount of [C] is the combined amount.
Accordingly, in step [III], in order to remove excess component [C] so that the amount of component [C] relative to component [A-2] falls within the above range, a suitable washing rate in step [II] is used. Is preferably selected.
Moreover, it is preferable not to provide a prepolymerization step between the steps [I] and [III].

The amount of component [A-1], component [A-2], [B] used in the present invention is arbitrary. For example, the usage-amount of component [A-1] with respect to component [B] becomes like this. Preferably it is 1.0 micromol-50 micromol with respect to 1 g of component [B], Most preferably, it is the range of 2.0 micromol-30 micromol.
Moreover, the usage-amount of component [A-2] becomes like this. Preferably it is 0.5 micromol-25 micromol with respect to 1 g of component [B], Most preferably, it is the range of 1.0 micromol-15 micromol.

The component [A-1] and the component [A-2] used in the present invention have a component [A-1] / component [A-2] molar ratio of 1.0 or more and 99.0 or less. By changing this ratio, it is possible to adjust the balance between melt physical properties and catalyst activity.
That is, from the component [A-1], a low molecular weight terminal vinyl macromer is produced, and from the component [A-2], a high molecular weight body obtained by copolymerizing a part of the macromer is produced.
Therefore, the macromer concentration can be changed by changing the ratio of the component [A-1] to the component [A-2], thereby changing the branching amount of the polymer.
In order to produce a more branched polymer, the molar ratio of component [A-1] / component [A-2] needs to be 1.0 or more, preferably 1.5 or more, More preferably, it is 2.0 or more. Further, the upper limit is 99.0 or less, preferably 40.0 or less, more preferably 10.0 or less, and in order to efficiently obtain the polymer of the present invention with high catalytic activity. , Preferably it is 5.0 or less, More preferably, it is the range of 3.0 or less. Here, component [A-1] indicates the amount of component [A-1] used in step [I], while component [A-2] is the amount of component [A-2] in step [III]. Indicates the amount used.
In addition, by using component [A-1] within the above range, it is possible to adjust the balance between the average molecular weight and the catalytic activity with respect to the amount of hydrogen.

3. Olefin Polymerization Catalyst The olefin polymerization catalyst according to the present invention is a solid catalyst obtained by using the above-described respective olefin polymerization catalyst components through the above-described steps. This catalyst contains at least component [A-1], component [A-2], component [B], and component [C]. This catalyst can increase the prepolymerization ratio as compared with the catalyst obtained by the production method proposed in Patent Documents 19 and 20, and as a result, the bulk density is high, the fluidity is high, and the handling is easy. This is a (prepolymerized) olefin polymerization catalyst.

In addition, the catalyst according to the present invention is preferable because it can be subjected to prepolymerization consisting of being polymerized in a small amount by bringing the olefin into contact therewith. By performing the preliminary polymerization, the particle properties are improved and handling becomes easy, and the melt physical properties can be improved when the main polymerization is performed.
The present inventors consider that the reason why the melt physical properties are improved is that the branched components can be uniformly distributed among the polymer particles when the main polymerization is performed.
Therefore, the amount of the polymer to be prepolymerized is preferably 0.01 or more, more preferably 0.1 or more by weight ratio with respect to the component [B], and the upper limit is 100 or less for economy and handling. Preferably it is 50 or less. Here, the weight ratio of the polymer to the component [B] may be expressed as the prepolymerization magnification.

The olefin used for the prepolymerization is not particularly limited, but propylene, ethylene, 1-butene, 1-hexene, 1-octene, 4-methyl-1-pentene, 3-methyl-1-butene, vinylcyclohexane. Examples include alkane and styrene, and propylene is preferable.
The olefin feed method may be any method such as a feed method for maintaining the olefin at a constant rate or a constant pressure in the reaction tank, a combination thereof, or a stepwise change. The prepolymerization temperature and time are not particularly limited, but are preferably in the range of −20 ° C. to 100 ° C. and 5 minutes to 24 hours, respectively. Moreover, component [C] can also be added at the time of prepolymerization. It is also possible to wash after the prepolymerization.
In addition to the component [A-1], the component [A-2], the component [B], and the component [C], the catalyst used in the present invention includes titania and the like as long as the object of the present invention is not impaired. A lubricant may be added.

4). Use of Catalyst / Olefin Polymerization The polymerization mode is such that the olefin polymerization catalyst including the component [A-1], the component [A-2], the component [B], and the component [C] efficiently contacts with the monomer. Any style can be adopted.
Specifically, a slurry method using an inert solvent, a so-called bulk method using a monomer itself (for example, propylene) as a solvent without using an inert solvent, a solution polymerization method, or substantially using no liquid solvent. A gas phase method for keeping each monomer in a gaseous state can be employed. Moreover, the method of performing continuous polymerization and batch type polymerization is also applied. In addition to single-stage polymerization, it is possible to carry out multistage polymerization of two or more stages.

In the case of slurry polymerization, a saturated aliphatic or aromatic hydrocarbon such as hexane, heptane, pentane, cyclohexane, benzene, toluene, or the like is used alone or as a polymerization solvent.
The polymerization temperature is 0 ° C. or higher and 150 ° C. or lower. In particular, when bulk polymerization is used, the temperature is preferably 40 ° C or higher, more preferably 50 ° C or higher. The upper limit is preferably 80 ° C. or lower, and more preferably 75 ° C. or lower.
Furthermore, when using vapor phase polymerization, 40 degreeC or more is preferable, More preferably, it is 50 degreeC or more. The upper limit is preferably 100 ° C. or lower, more preferably 90 ° C. or lower.

The polymerization pressure is 1.0 MPa or more and 5.0 MPa or less. In particular, when bulk polymerization is used, the pressure is preferably 1.5 MPa or more, more preferably 2.0 MPa or more. The upper limit is preferably 4.0 MPa or less, more preferably 3.5 MPa or less.
Furthermore, when using vapor phase polymerization, 1.0 MPa or more is preferable, and 1.5 MPa or more is more preferable. The upper limit is preferably 3.0 MPa or less, more preferably 2.5 MPa or less.

Furthermore, as a molecular weight regulator and for activity improvement effect, hydrogen is supplementarily used in a molar ratio of 1.0 × 10 ⁻⁶ or more and 1.0 × 10 ⁻² or less with respect to the monomer. be able to.
Also, by changing the amount of hydrogen used, in addition to the average molecular weight of the polymer to be produced, the molecular weight distribution, the deviation of the molecular weight distribution toward the high molecular weight side, very high molecular weight components, branching (amount, length, Distribution) can be controlled, whereby the melt physical properties such as strain hardening degree, melt tension, and melt spreadability can be controlled.
The olefin as a monomer that can be used in the present invention is an α-olefin having 2 to 20 carbon atoms. Examples of the olefin polymer include a single monomer homopolymer and a copolymer between two or more monomers. The olefin polymerization catalyst obtained from the method for producing an olefin polymerization catalyst of the present invention can be suitably used for homopolymerization of propylene and copolymerization of propylene and an α-olefin having 2 to 20 carbon atoms other than propylene. .

In addition to the propylene monomer, copolymerization using an α-olefin having about 2 to 20 carbon atoms (excluding those used as a monomer) as a comonomer may be performed. The (total) comonomer content in the propylene-based polymer is in the range of 0 mol% or more and 20 mol% or less, and a plurality of the above-mentioned comonomers can be used. Specifically, they are ethylene, 1-butene, 1-hexene, 1-octene and 4-methyl-1-pentene.
Among these, in order to obtain the propylene polymer according to the present invention in a good balance between melt properties and catalytic activity, it is preferable to use ethylene at 5 mol% or less. In particular, in order to obtain a polymer having high rigidity, it is preferable to use ethylene so that ethylene contained in the polymer is 1 mol% or less, and propylene homopolymerization is more preferable.

5. Analysis and Physical Properties of Olefin Polymer In the present invention, a component [A-1] having a specific structure produces a macromer having a vinyl structure at the terminal by β-methyl elimination reaction, and further, a component having a specific structure [ A-2] is characterized in that the macromer is copolymerized to produce a polymer having a long-chain branched structure.
Therefore, the olefin polymer that can be produced according to the present invention is characterized in that it is a polymer in which many long-chain branches are introduced. Moreover, it can be inferred that the introduction of a lot of long-chain branches further improves the melt physical properties and is advantageous for various moldings.
Examples of the method for quantifying the amount of long chain branching include measurement methods using ¹³ C-NMR and 3D-GPC shown below.
In the present invention, the amount of long chain branching was evaluated using the branching index (g ′) calculated from the 3D-GPC measurement shown below.

[Branch structure analysis by 3D-GPC]
In this specification, 3D-GPC refers to a GPC device to which three detectors are connected. Three such detectors are a differential refractometer (RI), a viscosity detector (Viscometer) and a multi-angle laser light scattering detector (MALLS).
Waters Alliance GPCV2000 was used as a GPC apparatus equipped with a differential refractometer (RI) and a viscosity detector (Viscometer).
In addition, as a light scattering detector, a DAWN-E manufactured by Wyatt Technology, a multi-angle laser light scattering detector (MALLS) was used.
The detectors were connected in the order of MALLS, RI, and Viscometer. The mobile phase solvent is 1,2,4-trichlorobenzene (antioxidant Irganox 1076 added at a concentration of 0.5 mg / mL). The flow rate is 1 mL / min. As the column, two Tosoh Corporation GMHHR-H (S) HT were connected and used. The temperature of the column, sample injection section, and each detector is 140 ° C. The sample concentration was 1 mg / mL. The injection volume (sample loop volume) is 0.2175 mL.
In order to obtain the absolute molecular weight (M) obtained from MALLS, the radius of inertia (Rg), and the intrinsic viscosity ([η]) obtained from Viscometer, data processing software ASTRA (version 4.73.04) attached to MALLS was used. The calculation was performed with reference to the following documents.

References:
1. Developments in polymer characterization, vol. 4). Essex: Applied Science; 1984. Chapter 1.
2. Polymer, 45, 6495-6505 (2004).
3. Macromolecules, 33, 2424-2436 (2000)
4). Macromolecules, 33, 6945-6952 (2000)

[Calculation of branching index (g ′)]
The branching index (g ′) is a ratio (ηbranch / ηlin) between the intrinsic viscosity (ηbranch) obtained by measuring the sample with the above Viscometer and the intrinsic viscosity (ηlin) obtained separately by measuring a linear polymer. ,calculate.
When long chain branching is introduced into a polymer molecule, the radius of inertia is reduced compared to a linear polymer molecule having the same molecular weight. Since the intrinsic viscosity becomes smaller when the radius of inertia becomes smaller, the ratio of the intrinsic viscosity (ηbranch) of the branched polymer to the intrinsic viscosity (ηbrin) of the linear polymer having the same molecular weight (ηbranch / ηlin) as long chain branching is introduced Is getting smaller.
Therefore, when the branching index (g ′ = ηbranch / ηlin) is smaller than 1, it means that a branch is introduced, and as the value decreases, the introduced long chain branch increases. Means to do.

The olefin polymer that can be produced by the present invention is characterized in that many long-chain branches are introduced, thereby improving the melt physical properties.
Therefore, in the olefin polymer according to the present invention, the branching index (g ′) is characterized by 0.95 or less at a molecular weight (M) of 1,000,000, and further 0.90 or less. And

  EXAMPLES Next, although an Example demonstrates this invention further more concretely, this invention is not limited to a following example, unless the summary is exceeded. In addition, the physical-property measurement, analysis, etc. in a following example follow the following method.

(1) Melt flow rate (MFR)
It was measured according to the melt flow rate (test condition: 230 ° C., load 2.16 kgf) of the polypropylene test method of JIS K6758. The unit is g / 10 minutes.
(2) Branched structure analysis by 3D-GPC It was performed by the method described in the present specification.

[Synthesis example 1 of catalyst component [A-1]]
(1) Synthesis of dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-i-propylphenyl) indenyl}] hafnium: (component [A-1] (Synthesis of Complex 1):
(1-1) Synthesis of 4- (4-i-propylphenyl) indene:
To a 500 ml glass reaction vessel, add 15 g (91 mmol) of 4-i-propylphenylboronic acid and 200 ml of dimethoxyethane (DME), add a solution of 90 g (0.28 mol) of cesium carbonate and 100 ml of water, and add 4-bromoindene. 13 g (67 mmol) and tetrakistriphenylphosphinopalladium 5 g (4 mmol) were sequentially added, and the mixture was heated at 80 ° C. for 6 hours.
After allowing to cool, the reaction solution was poured into 500 ml of distilled water, transferred to a separatory funnel, and extracted with diisopropyl ether. The ether layer was washed with saturated brine and dried over sodium sulfate. Sodium sulfate was filtered, the solvent was distilled off under reduced pressure, and the residue was purified by a silica gel column to obtain 15.4 g (yield 99%) of 4- (4-i-propylphenyl) indene as a colorless liquid.

(1-2) Synthesis of 2-bromo-4- (4-i-propylphenyl) indene:
To a 500 ml glass reaction vessel, 15.4 g (67 mmol) of 4- (4-i-propylphenyl) indene, 7.2 ml of distilled water and 200 ml of DMSO were added, and 17 g (93 mmol) of N-bromosuccinimide was gradually added thereto. . The mixture was stirred at room temperature for 2 hours, poured into 500 ml of ice water, and extracted three times with 100 ml of toluene. The toluene layer was washed with saturated brine, 2 g (11 mmol) of p-toluenesulfonic acid was added, and the mixture was heated to reflux for 3 hours while removing moisture. The reaction mixture was allowed to cool, washed with saturated brine, and dried over sodium sulfate. Sodium sulfate was filtered, the solvent was distilled off under reduced pressure, and the residue was purified with a silica gel column to obtain 19.8 g (yield 96%) of 2-bromo-4- (4-i-propylphenyl) indene as a yellow liquid. .

(1-3) Synthesis of 2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indene:
To a 500 ml glass reaction vessel, 6.7 g (82 ml 1 mol) of 2-methylfuran and 100 ml of DME were added and cooled to -70 ° C. in a dry ice-methanol bath. To this, 51 ml (81 mmol) of a 1.59 mol / L n-butyllithium-n-hexane solution was added dropwise and stirred as it was for 3 hours. The solution was cooled to −70 ° C., and a solution of 20 ml (87 mmol) of triisopropyl borate and 50 ml of DME was added dropwise thereto. After dropping, the mixture was stirred overnight while gradually returning to room temperature.
After the reaction solution was hydrolyzed with 50 ml of distilled water, a solution of 223 g of potassium carbonate and 100 ml of water and 19.8 mg (63 mmol) of 2-bromo-4- (4-i-propylphenyl) indene were added in this order, and the mixture was heated at 80 ° C. The mixture was heated and reacted for 3 hours while removing low-boiling components. After allowing to cool, the reaction solution was poured into 300 ml of distilled water, transferred to a separatory funnel and extracted three times with diisopropyl ether. The ether layer was washed with saturated brine and dried over sodium sulfate. Sodium sulfate was filtered off, the solvent was distilled off under reduced pressure, and the residue was purified with a silica gel column to obtain 19.6 g of 2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indene as a colorless liquid ( Yield 99%).

(1-4) Synthesis of dimethylbis (2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indenyl) silane:
To a 500 ml glass reaction vessel, 9.1 g (29 mmol) of 2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indene and 200 ml of THF are added, and -70 in a dry ice-methanol bath. Cooled to ° C. To this, 17 ml (28 mmol) of a 1.66 mol / L n-butyllithium-hexane solution was dropped, and the mixture was stirred as it was for 3 hours. The mixture was cooled to −70 ° C., 0.1 ml (2 mmol) of 1-methylimidazole and 1.8 g (14 mmol) of dimethyldichlorosilane were sequentially added, and the mixture was stirred overnight while gradually returning to room temperature.
Distilled water was added to the reaction solution, transferred to a separatory funnel and washed with brine until neutral, and sodium sulfate was added to dry the reaction solution. Sodium sulfate was filtered, the solvent was distilled off under reduced pressure, and the residue was purified with a silica gel column, and dimethylbis (2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indenyl) silane was diluted lightly. 8.6 g (88% yield) of a yellow solid was obtained.

Synthesis of (1-5) dimethylsilylenebis (2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indenyl) hafnium dichloride:
To a 500 ml glass reaction vessel, 8.6 g (13 mmol) of dimethylbis (2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indenyl) silane and 300 ml of diethyl ether were added and dried. It cooled to -70 degreeC with the ice-methanol bath. Thereto was added dropwise 15 ml (25 mmol) of a 1.66 mol / L n-butyllithium-n-hexane solution, and the mixture was stirred for 3 hours. The solvent of the reaction solution was distilled off under reduced pressure, 400 ml of toluene and 40 ml of diethyl ether were added, and the solution was cooled to −70 ° C. in a dry ice-methanol bath. Thereto was added 4.0 g (13 mmol) of hafnium tetrachloride. Thereafter, the mixture was stirred overnight while gradually returning to room temperature.
The solvent was distilled off under reduced pressure and recrystallized from dichloromethane-hexane to obtain a racemic dimethylsilylenebis (2- (2-methyl-5-furyl) -4- (4-i-propylphenyl) indenyl) hafnium dichloride. As a yellow crystal, 7.6 g (yield 65%) was obtained.
The identified value by ^{1 H-NMR} of the obtained racemates are described below.
¹ H-NMR (C6D6) identification result Racemate: δ0.95 (s, 6H), δ1.10 (d, 12H), δ2.08 (s, 6H), δ2.67 (m, 2H), δ5. 80 (d, 2H), δ 6.37 (d, 2H), δ 6.74 (dd, 2H), δ 7.07 (d, 2H), δ 7.13 (d, 4H), δ 7.28 (s, 2H ), Δ 7.30 (d, 2H), δ 7.83 (d, 4H).

[Synthesis Example 2 of catalyst component [A-2]]:
(1) Synthesis of rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium: (synthesis of component [A-2] (complex 2) ):
The synthesis of rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium is carried out according to the method described in Example 1 of JP-A-11-240909. As well as.

[Synthesis Example of Catalyst Component [B]]
Chemical treatment of ion-exchange layered silicate:
In a separable flask, 96% sulfuric acid (668 g) was added to 2264 g of distilled water, and then 4 L of montmorillonite (Mizusawa Chemical Benclay SL: average particle size 19 μm) was added as a layered silicate. The slurry was heated at 90 ° C. for 210 minutes. The reaction slurry was filtered after adding 4000 g of distilled water to obtain 810 g of a cake-like solid.
Next, 432 g of lithium sulfate and 1924 g of distilled water were added to the separable flask to make a lithium sulfate aqueous solution, and the entire amount of the solid on the cake was charged. The slurry was reacted at room temperature for 120 minutes. 4 L of distilled water was added to this slurry, followed by filtration, further washing with distilled water to pH 5-6, and filtration. As a result, 760 g of a cake-like solid was obtained.
The obtained solid was preliminarily dried overnight at 100 ° C. under a nitrogen stream, and then coarse particles of 53 μm or more were removed and further dried at 200 ° C. for 2 hours under reduced pressure to obtain 220 g of chemically treated montmorillonite.
The composition of this chemically treated montmorillonite is Al: 6.45 wt%, Si: 38.30 wt%, Mg: 0.98 wt%, Fe: 1.88 wt%, Li: 0.16 wt%, Al / Si = 0.175 [mol / mol].

[Example 1]
Catalyst preparation and prepolymerization:
Into a three-necked flask (volume: 1 L), 10 g of the chemically treated montmorillonite obtained above was added, and heptane (66 mL) was added to form a slurry. 0.0 mL) was added and the mixture was stirred for 1 hour, and then washed with heptane until the residual liquid ratio became 1/100 to make the total volume 30 mL.
In another flask (volume: 200 mL), rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) prepared in Synthesis Example 1 of the catalyst component [A-1] was prepared. ) -4- (4-i-propylphenyl) indenyl}] hafnium (105 μmol) was dissolved in toluene (21 mL) (Solution 1), and the catalyst component [A- 2] rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in Synthesis Example 2 was dissolved in toluene (9 mL). (Solution 2).

After adding triisobutylaluminum (0.42 mmol: 0.6 mL of a heptane solution with a concentration of 143 mg / mL) to the 1 L flask containing the chemically treated montmorillonite, the above solution 1 (21 mL) was added and stirred for 20 minutes at room temperature. (V ₀ = 30 + 0.6 + 21 ml).
Thereafter, 250 ml (P ₁ ) of heptane was added and the mixture was allowed to settle after stirring, and 270 ml (d ₁ ) of the supernatant was extracted (washing rate = 0.10≈1 / 10, and the amount of residual aluminum was 0.042 mmol). Subsequently, 19 ml of toluene and 5.0 ml of heptane were added.
Thereafter, triisobutylaluminum (0.18 mmol: 0.25 mL of a heptane solution having a concentration of 143 mg / mL) was added, and then the above solution 2 was added, followed by stirring at room temperature for 1 hour (residual aluminum amount was 0.222 mmol, component [C] / component [A-2] = 4.9).
Thereafter, 190 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was set to 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 4 hours. Thereafter, propylene feed was stopped and residual polymerization was carried out for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 143 mg / mL) was added to the remaining portion and stirred for 5 minutes.
This solid was dried under reduced pressure for 1 hour to obtain 30.1 g of a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 2.01 (Catalyst A).

[Example 2]
Catalyst preparation and prepolymerization:
Into a three-necked flask (volume: 1 L), 10 g of the chemically treated montmorillonite obtained above was added, and heptane (66 mL) was added to form a slurry. 0.0 mL) was added and the mixture was stirred for 1 hour, and then washed with heptane until the residual liquid ratio became 1/100 to make the total volume 50 mL.
In another flask (volume: 200 mL), rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) prepared in Synthesis Example 1 of the catalyst component [A-1] was prepared. ) -4- (4-i-propylphenyl) indenyl}] hafnium (105 μmol) was dissolved in toluene (21 mL) (Solution 1), and the catalyst component [A- 2] rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in Synthesis Example 2 was dissolved in toluene (9 mL). (Solution 2).

After adding triisobutylaluminum (4.2 mmol: 5.9 mL of a heptane solution having a concentration of 143 mg / mL) to the 1 L flask containing the chemically treated montmorillonite, the above solution 1 (21 mL) was added and stirred at room temperature for 20 minutes. (V ₀ = 50 + 5.9 + 21 ml).
Thereafter, 230 ml (P ₁ ) of heptane was added and allowed to settle after stirring, 270 ml (d ₁ ) of the supernatant was extracted (W ₁ = 0.12), 270 ml (P ₂ ) of heptane was again added and allowed to settle after stirring. 270 ml (d ₂ ) of the supernatant was extracted (W ₂ = 0.12) (cleaning rate = 0.014≈1 / 100, the amount of residual aluminum is 0.042 mmol). Subsequently, 26 ml of toluene and 21 ml of heptane were added.
Thereafter, triisobutylaluminum (0.18 mmol: 0.25 mL of a heptane solution having a concentration of 143 mg / mL) was added, and then the above solution 2 was added, followed by stirring at room temperature for 1 hour (residual aluminum amount was 0.222 mmol, component [ C] / component [A-2] = 4.9).
Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was set to 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 4 hours. Thereafter, propylene feed was stopped and residual polymerization was carried out for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 143 mg / mL) was added to the remaining portion and stirred for 5 minutes.
This solid was dried under reduced pressure for 1 hour to obtain 30.3 g of a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 2.03 (Catalyst B).

[Comparative Example 1]
Catalyst preparation and prepolymerization:
Into a three-necked flask (volume: 1 L), 10 g of the chemically treated montmorillonite obtained above was added, and heptane (66 mL) was added to form a slurry. 0.0 mL) was added and the mixture was stirred for 1 hour, and then washed with heptane until the residual liquid ratio became 1/100 to make the total volume 50 mL.
In another flask (volume: 200 mL), rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) prepared in Synthesis Example 1 of the catalyst component [A-1] was prepared. ) -4- (4-i-propylphenyl) indenyl}] hafnium (105 μmol) was dissolved in toluene (21 mL) (Solution 1), and the catalyst component [A- 2] rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in Synthesis Example 2 was dissolved in toluene (9 mL). (Solution 2).

After adding triisobutylaluminum (0.42 mmol: 0.6 mL of a heptane solution with a concentration of 143 mg / mL) to the 1 L flask containing the chemically treated montmorillonite, the above solution 1 (21 mL) was added and stirred for 20 minutes at room temperature. did.
Thereafter, triisobutylaluminum (0.18 mmol: 0.25 mL of a heptane solution having a concentration of 143 mg / mL) was added, and then the above solution 2 was added, followed by stirring at room temperature for 1 hour (residual aluminum amount was 0.60 mmol, component [ C] / component [A-2] = 13.3.
Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was set to 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 4 hours. Thereafter, propylene feed was stopped and residual polymerization was carried out for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 143 mg / mL) was added to the remaining portion and stirred for 5 minutes.
This solid was dried under reduced pressure for 1 hour to obtain 26.1 g of a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 1.61 (Catalyst C).

[Comparative Example 2]
Catalyst preparation and prepolymerization:
Into a three-necked flask (volume: 1 L), 10 g of the chemically treated montmorillonite obtained above was added, and heptane (66 mL) was added to form a slurry. 0.0 mL) was added and the mixture was stirred for 1 hour, and then washed with heptane until the residual liquid ratio became 1/100 to make the total volume 50 mL.
In another flask (volume: 200 mL), rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) prepared in Synthesis Example 1 of the catalyst component (A-1) was prepared. ) -4- (4-i-propylphenyl) indenyl}] hafnium (105 μmol) in toluene (21 mL) (solution 1), and in another flask (volume 200 mL), the catalyst component (A- 2) rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in Synthesis Example 2 was dissolved in toluene (9 mL). (Solution 2).

After adding triisobutylaluminum (0.60 mmol: 0.84 mL of a heptane solution with a concentration of 143 mg / mL) to the 1 L flask containing the chemically treated montmorillonite, the above solution 1 (21 mL) was added and stirred for 5 minutes at room temperature. did.
Then, the above solution 2 was added, and the mixture was stirred at room temperature for 1 hour (the amount of residual aluminum was 0.60 mmol, component [C] / component [A-2] = 13.3).
Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was set to 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 4 hours. Thereafter, propylene feed was stopped and residual polymerization was carried out for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 143 mg / mL) was added to the remaining portion and stirred for 5 minutes.
This solid was dried under reduced pressure for 1 hour to obtain 25.0 g of a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of prepolymerized polymer by the amount of solid catalyst) was 1.50 (catalyst D).

  The outlines of Examples 1 and 2 and Comparative Examples 1 and 2 are summarized in Table 1.

[Polymerization Example 1]
Propylene polymerization:
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL), 76 Nml of hydrogen was introduced, 750 g of liquid propylene was introduced, and the temperature was raised to 70 ° C.
Thereafter, 80 mg of the catalyst A synthesized in Example 1 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, ethanol was added to terminate the polymerization.
As a result, 310 g of a polymer was obtained. The MFR was 1.4 g / 10 min, and the activity was 3900 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

[Polymerization Example 2]
In the polymerization example 1, the same polymerization was carried out except that the amount of hydrogen to be introduced was 57 Nml and the catalyst A was used in an amount of 90 mg.
As a result, 306 g of a polymer was obtained. The MFR was 0.6 g / 10 min, and the activity was 3400 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

[Polymerization Example 3]
In the polymerization example 1, instead of the catalyst A, the same polymerization was carried out except that 80 mg of the catalyst B synthesized in Example 2 was used.
As a result, 280 g of a polymer was obtained. The MFR was 1.1 g / 10 min, and the activity was 3500 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

[Polymerization Example 4]
Propylene polymerization:
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL), 76 Nml of hydrogen was introduced, 750 g of liquid propylene was introduced, and the temperature was raised to 70 ° C.
Thereafter, 100 mg of the catalyst C synthesized in Comparative Example 1 with a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, ethanol was added to terminate the polymerization.
As a result, 200 g of a polymer was obtained. The MFR was 0.8 g / 10 min, and the activity was 2000 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

[Polymerization Example 5]
In Polymerization Example 4, the same polymerization was carried out except that the amount of hydrogen to be introduced was 95 Nml.
As a result, 260 g of a polymer was obtained. The MFR was 2.0 g / 10 min, and the activity was 2600 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

[Polymerization Example 6]
In the polymerization example 4, instead of the catalyst C, the same polymerization was carried out except that 100 mg of the catalyst D synthesized in the comparative example 2 was used.
As a result, 200 g of a polymer was obtained. The MFR was 1.0 g / 10 min, and the activity was 2000 gPP / g catalyst · hour. The results are summarized in Table 2 and FIG.

  As is apparent from Table 2 and FIG. 2, the catalysts (A, B) obtained from the method for producing an olefin polymerization catalyst of the present invention are more active than the catalysts of the conventional methods (Comparative Examples 1 and 2). It can be seen that a propylene polymer containing a long chain branch can be efficiently produced.

[Synthesis Example 3 of catalyst component [A-1]]
Synthesis of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (complex 3):
The synthesis of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium is disclosed in JP 2009-57542 A. It carried out according to the method described in the publication.

[Synthesis Example 4 of catalyst component [A-2]]
Synthesis of rac-dichloro {dimethylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium (complex 4):
The synthesis of rac-dichloro {dimethylsilylenebis (2,3,5-trimethylcyclopentadienyl)} hafnium was carried out according to the method described in JP-A-1-319589.

[Example 3]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration heptane solution) was added, and then rac-dichloro [1,1′-, which had been adjusted to another flask (200 mL volume). A toluene solution (21 mL) of dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (0.105 mmol) was added.
Thereafter, 250 ml of heptane was added and the mixture was allowed to settle after stirring, and 270 ml of the supernatant was extracted (the washing rate was 1/10 and the amount of residual aluminum was 0.042 mmol). Subsequently, 19 ml of toluene and 5.0 ml of heptane were added.
After another 5 minutes, triisobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution) was added, and then rac-dichloro {dimethylsilylene bis ( 2,3,5-trimethylcyclopentadienyl)} hafnium (0.045 mmol) in toluene (9.0 mL) was added to form a slurry, and the mixture was stirred and reacted at room temperature for 60 minutes. Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 2 hours. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain 22.0 g of a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 1.20 (catalyst E).

[Comparative Example 3]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration heptane solution) was added, and then rac-dichloro [1,1′-, which had been adjusted to another flask (200 mL volume). Toluene solution (21 mL) of dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (0.105 mmol) was added, and after 5 minutes, After adding isobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution), rac-dichloro {dimethylsilylenebis (2,3,5) adjusted to another flask (volume 200 mL) was added. -Trimethylcyclopentadienyl)} hafnium (0.045 mmol) in toluene (9.0 mL) The solution was added to form a slurry, and the mixture was stirred for 60 minutes at room temperature to be reacted. Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 2 hours. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain 17.2 g of a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 0.72 (catalyst F).

[Synthesis Example 5 of catalyst component [A-2]]
Synthesis of rac-dichloro (1,1′-dimethylsilylenebis (2-methyl-4-phenylindenyl)) hafnium (complex 5):
The synthesis of rac-dichloro (1,1′-dimethylsilylenebis (2-methyl-4-phenylindenyl)) hafnium was performed according to Example 1 of JP-A-2001-253913.

[Example 4]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration heptane solution) was added, and then rac-dichloro [1,1′-, which had been adjusted to another flask (200 mL volume). A toluene solution (21 mL) of dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (0.105 mmol) was added.
Thereafter, 250 ml of heptane was added and the mixture was allowed to settle after stirring, and 270 ml of the supernatant was extracted (the washing rate was 1/10 and the amount of residual aluminum was 0.042 mmol). Subsequently, 19 ml of toluene and 5.0 ml of heptane were added.
After another 5 minutes, triisobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution) was added, and then the mixture was adjusted to another flask (volume: 200 mL). A solution of -dimethylsilylenebis (2-methyl-4-phenylindenyl)) hafnium (0.045 mmol) in toluene (9.0 mL) was added to give a slurry, and the mixture was stirred at room temperature for 60 minutes for reaction. Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 2 hours. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain 1.82 g of a dry prepolymerized catalyst. The preliminary weight ratio (value obtained by dividing the amount of prepolymerized polymer by the amount of solid catalyst) was 0.82 (catalyst G).

[Comparative Example 4]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration heptane solution) was added, and then rac-dichloro [1,1′-, which had been adjusted to another flask (200 mL volume). A toluene solution (21 mL) of dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (0.105 mmol) was added.
After another 5 minutes, triisobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution) was added, and then the mixture was adjusted to another flask (volume: 200 mL). A solution of -dimethylsilylenebis (2-methyl-4-phenylindenyl)) hafnium (0.045 mmol) in toluene (9.0 mL) was added to give a slurry, and the mixture was stirred at room temperature for 60 minutes for reaction. Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 2 hours. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain 13.2 g of a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of prepolymerized polymer by the amount of solid catalyst) was 0.32 (catalyst H).

[Synthesis Example 6 of catalyst component [A-1]]
Synthesis of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium (complex 6):
Synthesis of dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium is described in JP-A-2009-299046. Performed according to method.

[Synthesis Example 7 of catalyst component [A-2]]
Synthesis of rac-dichloro {1,1′-dimethylsilylene (2,3,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium (complex 7):
Synthesis of dichloro {1,1′-dimethylsilylene (2,3,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium is described in JP-A-2007-308486. It carried out according to the method of.

[Example 5]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration of heptane solution) was added, and then rac-dichloro [1,1′-dimethylsilylene prepared in another flask (volume 200 mL) was prepared. A toluene solution (21 mL) of bis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium (0.105 mmol) was added.
Thereafter, 250 ml of heptane was added and the mixture was allowed to settle after stirring, and 270 ml of the supernatant was extracted (the washing rate was 1/10 and the amount of residual aluminum was 0.042 mmol). Subsequently, 19 ml of toluene and 5.0 ml of heptane were added.
After another 5 minutes, triisobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution) was added, and then dichloro {1,1′-dimethylsilylene (200 mL) prepared in another flask (volume: 200 mL). 2,3,5-trimethylcyclopentadienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium (0.045 mmol) in toluene (9.0 mL) was added to make a slurry, The reaction was stirred for 60 minutes at room temperature. Thereafter, 220 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed for 4 hours while maintaining 40 ° C. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of prepolymerized polymer by the amount of solid catalyst) was 1.95 (catalyst I).

[Comparative Example 5]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Thereafter, triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration of heptane solution) was added, and then rac-dichloro [1,1′-dimethylsilylene prepared in another flask (volume 200 mL) was prepared. A toluene solution (21 mL) of bis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium (0.105 mmol) was added, and after another 5 minutes, triisobutylaluminum (0 18 mmol: dichloro {1,1′-dimethylsilylene (2,3,5-trimethylcyclopenta) prepared in another flask (volume 200 mL) after adding 140 mg / mL heptane solution (0.26 mL) Dienyl) (2-methyl-4-phenyl-4H-azurenyl)} hafnium (0. What was slurry was added with toluene (9.0 mL) solution of 45 mmol), and allowed to stir to react at room temperature for 60 minutes. Thereafter, 220 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed for 4 hours while maintaining 40 ° C. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 1.45 (catalyst J).

  The outline | summary of said Examples 3-5 and Comparative Examples 3-5 was put together in Table 3.

[Polymerization Example 7]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL), 19 Nml of hydrogen was added, 750 g of propylene was introduced, and the temperature was raised to 70 ° C.
Thereafter, 100 mg of the prepolymerized catalyst E synthesized in Example 3 above was weighted to the polymerization tank with high-pressure argon in a weight excluding the prepolymerized polymer, and polymerization was started. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 250 g of a polymer was obtained. The evaluation results are shown in Table 4.

[Polymerization Example 8]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquid propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst F synthesized in the above Comparative Example 3 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 304 g of polymer was obtained. The evaluation results are shown in Table 4.

[Polymerization Example 9]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL), 19 Nml of hydrogen was added, 750 g of propylene was introduced, and the temperature was raised to 70 ° C.
Thereafter, 100 mg of the prepolymerized catalyst G synthesized in Example 4 above was weighed excluding the prepolymerized polymer and pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 230 g of a polymer was obtained. The evaluation results are shown in Table 4.

[Polymerization Example 10]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquid propylene, the temperature was raised to 70 ° C.
Thereafter, 250 mg of the prepolymerized catalyst H synthesized in the above Comparative Example 4 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 313 g of a polymer was obtained. The evaluation results are shown in Table 4.

[Polymerization Example 11]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquefied propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst I synthesized in the above Example 5 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 300 g of a polymer was obtained. The evaluation results are shown in Table 4.

[Polymerization Example 12]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquefied propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst J synthesized in the above Comparative Example 5 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 214 g of a polymer was obtained. The evaluation results are shown in Table 4.

  As can be seen from Table 4, the catalysts (E, G, I) obtained from the method for producing an olefin polymerization catalyst of the present invention were prepared in the same manner as the catalysts A and B. 4 and 5), it can be seen that a propylene-based polymer having high activity and containing a long chain branch can be efficiently produced.

(Evaluation of properties of prepolymerization catalyst)
The prepolymerized catalyst was evaluated for bulk density and flowability.
The bulk density was measured by allowing the catalyst to fall freely from a height of 3 cm into a 10 ml volume container and rubbing the upper part to measure the filled weight to calculate the weight per unit volume.
In addition, the evaluation and measurement of the flowability were evaluated based on the following criteria for the passage of the catalyst through a metal funnel having a diameter of 12 mm.
○: Pass by giving vibration once.
Δ: Passed by applying vibration 2 to 3 times.
X: It does not pass even if it gives vibration three times or more.

  The evaluation results of the catalysts A to D are shown in Table 5. Table 6 shows the evaluation results of the catalysts E to J.

  As is clear from Table 5, the washed catalyst A and catalyst B have a larger prepolymerization ratio than the washed catalyst C and catalyst D, and as a result, the bulk density and the flowability of the catalyst are improved. I understand that.

  As is apparent from Table 6, the washed catalyst has a larger prepolymerization ratio than the corresponding washed catalyst, and as a result, the bulk density and the flowability of the catalyst are improved. Recognize.

[Synthesis Example 8 of catalyst component [A-1]]
(1) Synthesis of dichloro {1,1′-dimethylsilylene (2,3,4,5-tetramethylcyclopentadienyl) (2-isopropyl-4-phenyl-4H-azurenyl)} hafnium (complex 8):
Synthesis of dichloro {1,1′-dimethylsilylene (2,3,4,5-tetramethylcyclopentadienyl) (2-isopropyl-4-phenyl-4H-azurenyl)} hafnium is disclosed in JP 2009-40959. It implemented like the method of Example 1 of the gazette.

[Example 6]
Catalyst preparation and prepolymerization:
In a three-necked flask (volume: 1 L), 10 g of the ion-exchanged layered silicate chemically treated as described above is added, and 66 mL of heptane is added to form a slurry. 34 mL) was added and stirred for 1 hour, followed by washing with heptane (residual liquid ratio up to 1/100) to make the total volume 50 mL.
Triisobutylaluminum (0.42 mmol: 0.60 mL of a 140 mg / mL concentration of heptane solution) was then added, and then dichloro {1,1′-dimethylsilylene (2 , 3,4,5-tetramethylcyclopentadienyl) (2-isopropyl-4-phenyl-4H-azurenyl)} hafnium (0.105 mmol) in toluene (21 mL) was added.
Thereafter, 250 ml of heptane was added and the mixture was allowed to settle after stirring, and 270 ml of the supernatant was extracted (the washing rate was 1/10 and the amount of residual aluminum was 0.042 mmol). Subsequently, 19 ml of toluene and 5.0 ml of heptane were added.
Further, after 5 minutes, triisobutylaluminum (0.18 mmol: 0.26 mL of a 140 mg / mL concentration of heptane solution) was added, and then the catalyst component [A-2] was synthesized in another flask (volume: 200 mL). Rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in step 1 was added to a toluene (9 mL) solution to form a slurry. And stirred for 60 minutes at room temperature. Thereafter, 220 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was stabilized at 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed for 4 hours while maintaining 40 ° C. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (12 mmol: 8.5 mL of a 144 ml / mL heptane solution) was added to the portion remaining by the decantation and stirred for 10 minutes.
This solid was dried under reduced pressure for 2 hours to obtain 17.6 g of a dry prepolymerized catalyst. The prepolymerization ratio (a value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 0.76 (catalyst K).

[Comparative Example 6]
Catalyst preparation and prepolymerization:
Into a three-necked flask (volume: 1 L), 10 g of the chemically treated montmorillonite obtained above was added, and heptane (66 mL) was added to form a slurry. 0.0 mL) was added and the mixture was stirred for 1 hour, and then washed with heptane until the residual liquid ratio became 1/100 to make the total volume 50 mL.
In another flask (volume: 200 mL), the dichloro {1,1′-dimethylsilylene (2,3,4,5-tetramethylcyclopentadiene) prepared in Synthesis Example 1 of the catalyst component [A-1] was prepared. (Enyl) (2-isopropyl-4-phenyl-4H-azurenyl)} hafnium (105 μmol) is dissolved in toluene (21 mL) (solution 1), and the catalyst component [A -2] of rac-dichloro [1,1′-dimethylsilylenebis {2-methyl-4- (4-chlorophenyl) -4-hydroazurenyl}] hafnium (45 μmol) prepared in Synthesis Example 2 in toluene (9 mL) Dissolved (Solution 2).
After adding triisobutylaluminum (0.42 mmol: 0.6 mL of a heptane solution with a concentration of 143 mg / mL) to the 1 L flask containing the chemically treated montmorillonite, the above solution 1 (21 mL) was added and stirred for 20 minutes at room temperature. did.
Thereafter, triisobutylaluminum (0.18 mmol: 0.25 mL of a heptane solution having a concentration of 143 mg / mL) was added, and then the above solution 2 was added, followed by stirring at room temperature for 1 hour (residual aluminum amount was 0.60 mmol, component [ C] / component [A-2] = 13.3.
Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After the internal temperature of the autoclave was set to 40 ° C., propylene was fed at a rate of 5 g / hour, and prepolymerization was performed while maintaining the temperature at 40 ° C. for 4 hours. Thereafter, propylene feed was stopped and residual polymerization was carried out for 1 hour. After removing the supernatant of the obtained catalyst slurry by decantation, triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 143 mg / mL) was added to the remaining portion and stirred for 5 minutes.
This solid was dried under reduced pressure for 1 hour to obtain 12.6 g of a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of the prepolymerized polymer by the amount of the solid catalyst) was 0.26 (catalyst L).

  The outline of Example 6 and Comparative Example 6 is summarized in Table 7.

[Polymerization Example 13]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquefied propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst K synthesized in Example 6 above was fed into the polymerization tank with high-pressure argon in a weight excluding the prepolymerized polymer, and polymerization was started. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 192 g of a polymer was obtained. The evaluation results are shown in Table 8.

[Polymerization Example 14]
After thoroughly drying in advance by flowing nitrogen through a 3 L autoclave, the inside of the tank was replaced with propylene and cooled to room temperature. After adding 2.86 mL of a heptane solution of triisobutylaluminum (144 mg / mL) and introducing 750 g of liquefied propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst L synthesized in the above Comparative Example 5 in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization.
As a result, 140 g of a polymer was obtained. The evaluation results are shown in Table 8.

  As is clear from Table 8, the catalyst K obtained from the method for producing an olefin polymerization catalyst of the present invention, like the catalysts A and B, is more active than the catalyst of the conventional method (Comparative Example 6). It is high and it turns out that the propylene polymer containing a long chain branch can be manufactured efficiently.

(Evaluation of properties of prepolymerization catalyst)
Table 9 shows the evaluation results of the catalyst properties.

  As is apparent from Table 9, it can be seen that the washed catalyst K has a larger prepolymerization ratio than the catalyst L that is not washed, and as a result, the bulk density and the flowability of the catalyst are improved.

(Evaluation of macromer generation ability)
[Evaluation Example 1]
Evaluation of macromer-forming ability of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-i-propylphenyl) indenyl}] hafnium (complex 1):
(1) Preparation of catalyst In a three-necked flask (volume: 1 L), 10 g of chemically treated montmorillonite obtained by chemical treatment of the ion-exchanged layered silicate obtained above is added, and heptane (65 mL) is added to slurry. To this was added triisobutylaluminum (25 mmol: 34 mL of 142 mg / mL heptane solution), and the mixture was stirred for 1 hour, washed with heptane until the residual liquid became 1/100, and finally the total volume was reduced to 50 mL. It was prepared as follows.
In another flask (volume 200 mL), rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-isopropyl-phenyl) was added to toluene (30 mL). ) -Indenyl}] hafnium (complex 1) (0.15 mmol) was added to form a slurry solution.
Triisobutylaluminum (0.6 mmol: 0.86 mL of 142 mg / mL concentration of heptane solution) was added to the 1 L flask containing the previously chemically treated montmorillonite, and then the above slurry solution was added and stirred at room temperature for 60 minutes for reaction. . Thereafter, 170 mL of heptane was added, and this slurry was introduced into a 1 L autoclave.
After setting the internal temperature of the autoclave to 40 ° C., propylene was fed at a rate of 10 g / hour, and prepolymerization was performed while maintaining 40 ° C. for 2 hours. Thereafter, propylene feed was stopped, and residual polymerization was carried out at 40 ° C. for 1 hour. The resulting catalyst slurry supernatant was removed by decantation. Triisobutylaluminum (6 mmol: 8.5 mL of a heptane solution having a concentration of 142 mg / mL) was added to the portion remaining after the decantation, and the mixture was stirred for 10 minutes. This solid was dried under reduced pressure for 1 hour to obtain 22.3 g of a dry prepolymerized catalyst. The prepolymerization ratio (value obtained by dividing the amount of prepolymerized polymer by the amount of solid catalyst) was 1.23.

(2) Polymerization After 3L autoclave was heated and dried well by circulating nitrogen, the inside of the tank was replaced with propylene and cooled to room temperature. After charging 2.86 mL of a heptane solution of triisobutylaluminum (142 mg / mL) and introducing 750 g of liquid propylene, the temperature was raised to 70 ° C.
Thereafter, 200 mg of the prepolymerized catalyst in a weight excluding the prepolymerized polymer was pumped to the polymerization tank with high-pressure argon to initiate polymerization. After maintaining at 70 ° C. for 1 hour, unreacted propylene was quickly purged to terminate the polymerization. As a result, 140 g of a polymer was obtained.
Table 10 shows the evaluation results of the obtained polymer.

[Evaluation Example 2]
Evaluation of macromer-forming ability of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-t-butylphenyl) -indenyl}] hafnium (complex 3) :
In Evaluation Example 1, catalyst preparation and polymerization were performed in the same manner except that Complex 3 was used instead of Complex 1. As a result, 145 g of polymer was obtained.
Table 10 shows the evaluation results of the obtained polymer.

[Evaluation Example 3]
Evaluation of macromer-forming ability of rac-dichloro [1,1′-dimethylsilylenebis {2- (5-methyl-2-furyl) -4- (4-trimethylsilylphenyl) -indenyl}] hafnium (complex 6):
In Evaluation Example 1, catalyst preparation and polymerization were performed in the same manner except that Complex 6 was used instead of Complex 1. As a result, 135 g of a polymer was obtained.
Table 10 shows the evaluation results of the obtained polymer.

[Evaluation Example 4]
Evaluation of macromer-forming ability of dichloro {1,1′-dimethylsilylene (2,3,4,5-tetramethylcyclopentadienyl) (2-isopropyl-4-phenyl-4H-azurenyl)} hafnium (complex 8) :
In Evaluation Example 1, catalyst preparation and polymerization were performed in the same manner except that Complex 8 was used instead of Complex 1. As a result, 117 g of a polymer was obtained.
Table 10 shows the evaluation results of the obtained polymer.

  As can be seen from Table 10, all of Evaluation Examples 1 to 4 have a terminal vinyl ratio (Rv) of 0.75 or more, and in particular, Evaluation Examples 2 and 4 have high macromer generation ability.

  In the method for producing an olefin polymerization catalyst of the present invention, a propylene-based polymer containing a long-chain branch is obtained by sequentially performing specific steps using a catalyst component that produces a macromer and a catalyst component that copolymerizes the macromer. A highly active two-way catalyst that can be efficiently produced can be provided, and is highly industrially applicable. In addition, since the propylene polymer polymerized using the obtained highly active two-way catalyst is introduced with many long chain branches and has improved melt properties, it is also highly available. It is.

Claims (8)

A method for producing an olefin polymerization catalyst comprising at least the following components [A-1], [A-2], [B] and [C],
A method for producing an olefin polymerization catalyst, comprising sequentially performing the following steps [I] to [III].
Step [I]: A step of producing a contact product (1) by bringing component [A-1] into contact with components [B] and [C].
Step [II]: a step of washing the contact product (1) obtained in step [I] with an inert hydrocarbon solvent so that the washing rate is 1/10 or less to produce a washed product. .
However, the cleaning rate is determined by the following calculation formula.
W ₁ = (V ₀ + P ₁ −d ₁ ) / (V ₀ + P ₁ )
W ₂ = (V ₁ + P ₂ −d ₂ ) / (V ₁ + P ₂ )
_{W n = (V n-1} + P n -d n) / (V n-1 + P n)
Cleaning rate = W ₁ × W ₂ .. × W _n
In the calculation formula, the symbols have the following meanings.
W _n : Cleaning rate of the nth time (0 time indicates before cleaning, and W ₀ = 1)
V _n-1 : (n-1) Solution amount after the n-th washing d _n : Amount of solution extracted at the n-th washing P _n : Additional inert hydrocarbon solvent amount at the n-th washing step [III]: Step A step of producing a contact product (2) by bringing the component [A-2] into contact with the washed product obtained in [II].
However, the molar ratio [A-1] / [A-2] of [A-1] to component [A-2] is 1.0 to 99.0.
Component [A-1]: A metallocene compound that forms a polymerization catalyst for producing an olefin macromer. However, a metallocene compound that forms a polymerization catalyst for generating an olefin macromer generates a propylene homopolymer having a terminal vinyl ratio (Rv) of 0.5 or more when propylene homopolymerization is performed at 70 ° C. It is a metallocene compound that forms a polymerization catalyst.
Here, the terminal vinyl ratio (Rv) is defined by the following formula.
Rv = Mn / 21000 × [Vi]
(In the formula, Mn is the number average molecular weight determined by GPC, and [Vi] is the number of terminal vinyl groups per 1000 C calculated from ¹³ C-NMR.)
Component [A-2]: Compound represented by the general formula (a2).

[In General Formula (a2), E ²¹ and E ²² are each independently a cyclopentadienyl group, an indenyl group, a fluorenyl group, or an azulenyl group, and each may have a substituent (provided that The substituent is not a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur.) Q ²¹ represents a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or a germylene group optionally having a hydrocarbon group having 1 to 20 carbon atoms, and M ²¹ represents zirconium or hafnium. , X ²¹ and Y ²¹ are each independently a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, a silyl group having a hydrocarbon group having 1 to 20 carbon atoms, or a halogen having 1 to 20 carbon atoms. Represents a hydrocarbyl group, an amino group, or an alkylamino group having 1 to 20 carbon atoms. ]
Component [B]: an ionic compound or Lewis acid [B-] capable of reacting with the aluminum oxy compound [B-1], the transition metal compounds [A-1] and [A-2] to be converted into a cation. 2], at least one selected from the group consisting of solid acid fine particles [B-3] and ion-exchange layered silicate [B-4].
Component [C]: an organoaluminum compound. Component [A-1] is a compound represented by general formula (a1), The manufacturing method of the catalyst for olefin polymerization of Claim 1 characterized by the above-mentioned.

[In General Formula (a1), R ¹¹ and R ¹² each independently represent a heterocyclic group having 4 to 16 carbon atoms containing nitrogen, oxygen or sulfur. R ¹³ and R ¹⁴ each independently represent halogen, silicon, oxygen, sulfur, nitrogen, boron, phosphorus, or a C 6-16 aryl that may contain a plurality of hetero elements selected from these Or a heterocyclic group having 6 to 16 carbon atoms containing nitrogen, oxygen or sulfur. Further, M ¹¹ represents zirconium or hafnium, and X ¹¹ and Y ¹¹ each independently represent a hydrogen atom, a halogen atom, a hydrocarbon group having 1 to 20 carbon atoms, or a hydrocarbon group having 1 to 20 carbon atoms. A silyl group, a halogenated hydrocarbon group having 1 to 20 carbon atoms, an amino group or an alkylamino group having 1 to 20 carbon atoms, Q ¹¹ is a divalent hydrocarbon group having 1 to 20 carbon atoms, carbon number It represents a silylene group or a germylene group which may have 1 to 20 hydrocarbon groups. ] Component [A-1] is a compound represented by general formula (a3), The manufacturing method of the catalyst for olefin polymerization of Claim 1 characterized by the above-mentioned.

[In General Formula (a14), R ^{141 to} R ¹⁴⁴ are each independently a hydrocarbon group having 1 to 12 carbon atoms, a halogenated hydrocarbon group, or a silicon-containing hydrocarbon group, and R ¹⁴¹ and R ¹⁴² and / Or R ¹⁴³ and R ¹⁴⁴ may combine to form a divalent group, and R ¹⁴⁵ represents a hydrocarbon group having 1 to 10 carbon atoms, a silicon-containing hydrocarbon group having 1 to 10 carbon atoms, or A halogenated hydrocarbon group having 1 to 10 carbon atoms, and R ¹⁴⁶ is an aryl group having 6 to 30 carbon atoms, which may contain halogen, silicon, or a plurality of heteroelements selected therefrom. . Q ¹⁴¹ is a binding group that bridges two conjugated five-membered ring ligands, and is a divalent hydrocarbon group having 1 to 20 carbon atoms, a silylene group or carbon having a hydrocarbon group having 1 to 20 carbon atoms. Represents a germylene group having a hydrocarbon group of 1 to 20, M ¹⁴¹ represents zirconium or hafnium, and X ¹⁴¹ and Y ¹⁴¹ each independently represent a hydrogen atom, a halogen atom, or a carbon atom having 1 to 20 carbon atoms. Hydrogen group, alkoxy group having 1 to 20 carbon atoms, alkylamide group having 1 to 20 carbon atoms, trifluoromethanesulfonic acid group, phosphorus-containing hydrocarbon group having 1 to 20 carbon atoms, or silicon-containing hydrocarbon having 1 to 20 carbon atoms Represents a group. ]   The method for producing an olefin polymerization catalyst according to any one of claims 1 to 3, wherein the component [B] is an ion-exchange layered silicate [B-4].   The method for producing an olefin polymerization catalyst according to any one of claims 1 to 4, wherein the ion-exchange layered silicate [B-4] is a smectite group. M ^{21 of} component [A-2] is hafnium, The manufacturing method of the catalyst for olefin polymerization of any one of Claims 1-5 characterized by the above-mentioned.   The method for producing a catalyst for olefin polymerization according to any one of claims 1 to 6, wherein the olefin is preliminarily polymerized in a weight ratio of 0.01 to 100 with respect to the component [B]. .   The molecular weight (M) is used for the production of an olefin polymer having a branching index (g ′) of 0.95 or less at 1 million (log M = 6). The manufacturing method of the catalyst for olefin polymerization of description.

Images