JP2003342215A - Magnesium compound, solid catalyst component for polymerizing olefin, catalyst for polymerizing olefin and method for producing polyolefin - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To obtain a magnesium compound giving a nearly spherical olefin polymer having a narrow particle diameter distribution without deteriorating catalytic performances such as stereoregularity and polymerization activity, to obtain a solid catalyst component for polymerizing an olefin, to obtain a catalyst for polymerizing the olefin, and to provide a method for producing the polyolefin. <P>SOLUTION: The magnesium compound is obtained by reacting metal magnesium whose average particle diameter corresponding to an accumulated weight fraction of 50% is 50 to 2,000 μm, with an alcohol in a molar ratio of 4 to 40 to mole of the metal magnesium, and a halogen and/or a halogen-containing compound which contains the halogen atom in an amount of ≥0.0001 gram atom per gram atom of the metal magnesium in a stirring tank having a stirring shaft on which a stirring blade having a blade diameter (d) is disposed, while stirring the reaction mixture at a revolution rate (n), wherein n<SP>3</SP>d<SP>2</SP>is 4.3×10<SP>3</SP>to 4.0×10<SP>6</SP>. <P>COPYRIGHT: (C)2004,JPO

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to a magnesium compound, a solid catalyst component for olefin polymerization, a catalyst for olefin polymerization, and a method for producing a polyolefin.

[0002]

2. Description of the Related Art Conventionally, in the field of olefin polymerization catalysts for homopolymerizing or copolymerizing olefins such as ethylene or propylene, there has been widely used a technique in which a magnesium compound such as magnesium chloride or magnesium alkoxide is used as a carrier raw material without crushing. It has been carried out, and the improvement of the catalytic activity and the improvement of the powder form of the olefin polymer have been attempted.

For example, JP-A-63-280707 discloses a method of supporting a magnesium compound on an inorganic oxide such as silica for the purpose of improving the morphology of the olefin polymer such as particle size and shape. Also,
Japanese Patent Laid-Open No. 58-000811 discloses a method in which a magnesium compound is once dissolved in a solvent such as alcohol and then re-precipitated, which is used. However, these methods are extremely complicated in terms of steps because treatments such as loading, dissolution and precipitation of the magnesium compound are essential. In addition, these methods have a drawback that the catalyst performance is not stable, such that only the catalytic activity at the initial stage of polymerization is high.

Further, Japanese Patent Application Laid-Open No. 4-130107 discloses a method of using a magnesium compound obtained by reacting metallic magnesium, alcohol and a specific amount of halogen as a catalyst carrier. However, in this method, depending on the production conditions of the magnesium compound,
The particle size distribution and sphericity of the resulting polymer powder were not always sufficient.

[0005]

SUMMARY OF THE INVENTION The present invention has been made from the above point of view, and has a narrow particle size distribution and a nearly spherical olefin polymer without deteriorating the catalytic performance such as stereoregularity and polymerization activity. It is an object of the present invention to provide a magnesium compound that gives the above, a solid catalyst component for olefin polymerization, a catalyst for olefin polymerization, and a method for producing polyolefin.

As a result of intensive studies to achieve the above-mentioned object, the present inventors have identified a specific amount of magnesium metal having a specific average particle diameter, a specific amount of alcohol, and a halogen and / or a halogen-containing compound. The inventors have found that the above problems can be solved by reacting a magnesium compound produced by reacting under stirring conditions and a titanium compound to produce a solid catalyst component for olefin polymerization, and have completed the present invention.

[0007]

According to the first aspect of the present invention, the average particle diameter (D) corresponding to a cumulative weight fraction of 50% is obtained.
₅₀ ) 50-2000 μm metallic magnesium, alcohol having a molar ratio (ROH / Mg) of 4-40 with respect to 1 mol of metallic magnesium, and halogen containing 0.0001 gram atom or more halogen atom per 1 gram atom of metallic magnesium. And / or reacting the halogen-containing compound with stirring at a rotation speed n (times / minute) in a stirring tank having a stirring shaft in which a stirring blade having a blade diameter d (m) is arranged,
A magnesium compound obtained by stirring and reacting so that n ³ d ² becomes 4.3 × 10 ^{3 to} 4.0 × 10 ⁶ is provided.

According to a second aspect of the present invention, (a) the magnesium compound obtained by the above production method, and (b)
Provided is a method for producing a solid catalyst component for olefin polymerization obtained by reacting a titanium compound.

According to the third aspect of the present invention, there is provided an olefin polymerization catalyst comprising the following compounds [A] and [B] or the following compounds [A], [B] and [C]. [A] Solid catalyst component for olefin polymerization [B] Organoaluminum compound [C] Electron-donating compound

According to a fourth aspect of the present invention, there is provided a method for producing a polyolefin using the above-mentioned olefin polymerization catalyst.

According to the fifth aspect of the present invention, the average particle diameter (D ₅₀ ) corresponding to a cumulative weight fraction of 50% is 50 to 2
000 μm of metallic magnesium, alcohol having a molar ratio (ROH / Mg) of 4 to 40 to 1 mol of metallic magnesium, and 0.
A halogen and / or a halogen-containing compound containing a halogen atom of 0001 gram atom or more is rotated in a stirring tank having a stirring shaft in which a stirring blade having a blade diameter d (m) is arranged, and the rotation speed is n.
When the reaction is performed with stirring at (times / minute), n ³ d ² is 4.
Provided is a method for producing a magnesium compound, which is stirred and reacted so as to have a concentration of 3 × 10 ^{3 to} 4.0 × 10 ⁶ .

[0012]

BEST MODE FOR CARRYING OUT THE INVENTION Next, each catalyst component used in the present invention will be described. The following are preferred examples, and the present invention is not limited to these. 1. Catalyst Component [A] Solid Catalyst Component for Olefin Polymerization (a) Magnesium Compound In the present invention, the magnesium compound (a) has an average particle diameter (D ₅₀ ) of 50 corresponding to a cumulative weight fraction of 50%.
To 2000 μm of metal magnesium, alcohol having a molar ratio (ROH / Mg) of 4 to 40 to 1 mol of metal magnesium, and halogen and / or halogen containing 0.0001 gram atom or more of halogen atom to 1 gram atom of metal magnesium. When the contained compound is reacted by stirring at a rotation speed n (times / minute) in a stirring tank having a stirring shaft provided with a stirring blade having a blade diameter d (m), n ³ d ² is 4. The compound obtained by stirring and reacting so that it may be set to 3 * 10 < ³ > -4.0 * 10 < ⁶ > is used. D ₅₀ , ROH /
If Mg and n ³ d ² are out of the above ranges, the particle size distribution of the obtained polymer powder may be wide, or the sphericity may be reduced or the particles may aggregate. Conjecturely, for D ₅₀ , the reason for this is considered as follows. Magnesium compounds are tabular aggregates, and magnesium compounds are balanced by the balance between reaction speed (promoting tabular crystal aggregation) and particle-particle collisions, particle-wall collisions, or shearing from fluid (crystal aggregation suppression). The particle size and shape of the From this point, a more uniform reaction can be obtained when the reaction starts all at once. In general, the smaller particle size has a higher reaction rate in terms of specific surface area, but the smaller particle size magnesium has more coatings. This point is considered to affect the homogeneity of the reaction.
As for ROH / Mg, it is speculated, but if the magnesium concentration is too high, stirring nonuniformity occurs, and if it is too dilute, collision between particles becomes insufficient, which is not preferable.
As for n ³ d ^2, it is speculated that weak agitation results in non-uniform flow resulting in non-uniform reactions. on the other hand,
It is considered that even if the stirring is too strong, it becomes difficult to even agglomerate the plate-like crystals of the produced magnesium compound. D ₅₀ is preferably 75 to 1800 μm, and ROH / Mg is
It is preferably 5 to 20, and n ³ d ² is preferably 1.3 × 10 ^{4 to} 8.4 × 10 ⁵ . Such metallic magnesium having an average particle diameter (D ₅₀ ) of ₅₀ to 2000 μm can be produced by mechanical pulverization, cutting, melting, spraying or the like. Further, the blade diameter d and the stirring number n are not particularly limited, and can be appropriately adjusted within the range where n ³ d ² satisfies the above requirements. In this case, as the stirring blade,
Maxblend wing, full zone wing, paddle (flat blade)
Any blade, inclined blade blade, turbine blade, anchor blade or the like may be used as long as it is used for slurry mixing and stirring. Further, it may be used in a general form or in a multi-stage form. A plurality of baffles (baffles) along the axial direction may be arranged on the side surface of the wall of the stirring tank. Among these, stirring with a Maxblend blade equipped with a baffle is particularly preferable.

The shape of metallic magnesium is not particularly limited as long as it satisfies the above-mentioned requirement of the average particle diameter (D ₅₀ ). Therefore, it is possible to use any particle shape, for example, metallic magnesium having a granular shape, a ribbon shape, a powder shape, or the like.

As the alcohol, it is preferable to use a lower alcohol having 1 to 6 carbon atoms. In particular, the use of ethanol is preferable because a solid product that significantly improves the expression of catalytic performance can be obtained. The purity and water content of the alcohol are not particularly limited, but when an alcohol having a high water content is used, a film of magnesium hydroxide is formed on the surface of the magnesium metal, so that the water content is 1% or less, particularly 2,000.
It is preferable to use 0 ppm or less of alcohol. Further, in order to obtain an olefin polymer having a better morphology, the smaller the water content, the more preferable, and generally 200 ppm or less is desirable.

As the halogen, chlorine, bromine or iodine, particularly iodine is preferably used. The halogen atom of the halogen-containing compound is preferably chlorine, bromine or iodine.
Further, among the halogen-containing compounds, halogen-containing metal compounds are particularly preferable. As the halogen-containing compound, specifically, MgCl ₂ , MgI ₂ , Mg (OEt) C
1, Mg (OEt) I, MgBr ₂ , CaCl ₂ , Na
Cl, KBr and the like can be preferably used. Among these,
MgCl ₂ is particularly preferable. These states, shapes, particle sizes, etc. are not particularly limited and may be arbitrary, and for example, they can be used as a solution in an alcohol solvent (for example, ethanol). Iodine or MgCl ₂ is preferred,
It is speculated that this is because the effect of improving the solubility of the magnesium compound in ethanol is high.

In the halogen or the halogen-containing compound, the halogen atom in the halogen or the halogen-containing compound is 0.0001 gram atom or more, preferably 0.0005 gram atom or more, and more preferably 0.001 gram atom per 1 gram atom of metallic magnesium. Use an amount of at least gram atoms. If it is less than 0.0001 gram atom, when the obtained magnesium compound (a) is used as a carrier for the solid catalyst component, the polymerization activity and the particle shape of the olefin polymer become poor.

In the present invention, the halogen and the halogen-containing compound may be used alone or in combination of two or more kinds. Further, halogen and a halogen-containing compound may be used in combination. When halogen and a halogen-containing compound are used in combination, the amount of all halogen atoms in the halogen and the halogen-containing compound is 0.0001 gram atom or more, preferably 0.0005 gram atom or more, based on 1 gram atom of metal magnesium, and Preferably, an amount of 0.001 gram atom or more is used.

The upper limit of the amount of halogen and / or halogen-containing compound used is not particularly limited, and may be appropriately selected within the range where the magnesium compound (a) of the present invention can be obtained. Generally, it is preferred to use an amount of less than 0.06 gram atom.

In the present invention, the particle size of the magnesium compound (a) can be freely controlled during production of the magnesium compound (a) by appropriately selecting the amount of halogen and / or halogen-containing compound used within the above range. .

[0020] In the production of the magnesium compound (a), usually, metallic magnesium having the above average particle diameter _{(D 50),} the molar ratio of the (ROH / Mg) halogen and an alcohol, and the gram atom ratio of / Alternatively, the halogen-containing compound is reacted under the above-mentioned stirring conditions until generation of hydrogen gas is not observed (usually 10 to 30 hours). Specifically, when iodine is used as the halogen, a method in which solid iodine is added to an alcohol solution of metallic magnesium and then heated to react, an alcohol solution of iodine is added to an alcohol solution of metallic magnesium. It can be produced by a method of dropping and then reacting by heating, a method of dropping and reacting an alcohol solution of iodine while heating an alcohol solution of metallic magnesium.

Any of the methods may be carried out in an inert gas (eg, nitrogen gas, argon gas) atmosphere, optionally using an inert organic solvent (eg, saturated hydrocarbon such as n-hexane). preferable.

The reaction temperature of metallic magnesium, alcohol, and halogen and / or halogen-containing compound is usually 30 to 90 ° C. Preferably 30-60
C, and the performance is improved in this temperature range. This is speculated, but it is considered that the reaction rate and the solubility are excellent in balance, and a uniform magnesium compound is produced.

Regarding the addition of metallic magnesium, alcohol, and halogen and / or halogen-containing compounds,
It is not necessary to add the entire amount from the beginning, and it is possible to add the amount separately. For example, there is a method in which the entire amount of alcohol is charged from the beginning and metallic magnesium is charged in several times. In such a case, it is possible to prevent a temporary large amount of hydrogen gas from being generated, which is desirable from the viewpoint of safety.
Also, the reaction tank can be downsized. Further, it becomes possible to prevent entrainment of alcohol, halogen, etc., which is caused by the temporary large amount of hydrogen gas generation. The number of divisions may be determined in consideration of the scale of the reaction tank, and is not particularly limited, but considering the complexity of the operation, usually 5 to 10 times is preferable.

The reaction itself may be a batch type or a continuous type. Furthermore, as a modified method, a small amount of metallic magnesium is first added to the alcohol that has been entirely added from the beginning, the product produced by the reaction is separated and removed in another tank, and then a small amount of metallic magnesium is added again. It is also possible to repeat.

When the magnesium compound (a) thus obtained is used for preparing the solid catalyst component [A],
What was dried may be used, and what was washed with an inert solvent such as heptane after filtration may be used.

In any case, the magnesium compound (a) of the present invention can be used as a carrier for the solid catalyst component without performing operations such as pulverization or classification for making the particle size distribution uniform. The magnesium compound (a) of the present invention is nearly spherical, has a sharp particle size distribution, and has a small variation in sphericity from particle to particle.

The magnesium compound (a) usually has a particle size distribution index (P) represented by the following formula (I) of 3.4.
Less than, preferably less than 3.2. _{P '= (D 90 / D} 10) ····· (I) [ _{wherein, D 90} represents the particle diameter of the magnesium compound which cumulative weight fraction corresponding to 90% _{(a), D 10} is Shows the particle diameter of the magnesium compound (a) corresponding to a cumulative weight fraction of 10%. When the magnesium compound (a) having such a particle size distribution index (P) is used, a polymer having a higher polymerization activity and an excellent particle morphology can be obtained. The particle size distribution index (P) indicates the degree of spread of the particle size distribution of the magnesium compound (a). The smaller this value, the narrower and sharper the particle size distribution, and the more uniform the particle size of magnesium. It means that a large amount of the compound (a) is contained.

The magnesium compound (a) has a sphericity (S) represented by the following formula (II) of usually less than 1.30, preferably less than 1.28. S = (L ₁ / L ₂ ) ³ (II) [In the formula, L ₁ represents the longest diameter of the projected view of the magnesium compound, which is obtained by image processing with a scanning electron microscope and image processing. , L ₂ represents the diameter of a circle equal to the projected area of the magnesium compound. The magnesium compound (a) having such a sphericity (S) is preferable from the viewpoint of catalytic activity and morphology of polymer particles. The sphericity (S) indicates the degree of sphere of the object, and indicates that the object of S = 1 is a true sphere. Therefore, the closer S is to 1, the closer each particle of the magnesium compound (a) is to a true sphere. Such a magnesium compound (a) having a particle size distribution index (P) of less than 3.4 and a sphericity (S) of less than 1.30 is a metal magnesium, an alcohol, and a halogen and / or a halogen-containing compound as described above. Can be produced by reacting under the stirring conditions described above.

The magnesium compound (a) may be used alone, or two or more kinds produced under different conditions may be used in combination.

Such a magnesium compound (a) is
It is solid and consists essentially of magnesium alkoxide. Specific examples of magnesium alkoxide include dimethoxy magnesium, diethoxy magnesium, dipropoxy magnesium, dibutoxy magnesium, dihexyloxy magnesium, dioctoxy magnesium,
Dialkoxy magnesium and diaryloxy magnesium such as diphenoxy magnesium and dicyclohexyloxy magnesium; butoxy magnesium chloride, cyclohexyloxy magnesium chloride, phenoxy magnesium chloride, ethoxy magnesium chloride,
Examples thereof include alkoxy magnesium halides such as ethoxy magnesium bromide, butoxy magnesium bromide and ethoxy magnesium iodide, and aryloxy magnesium halides. Among these, dialkoxymagnesium is preferable, and diethoxymagnesium is particularly preferable in that a solid catalyst component having remarkably improved catalytic performance can be obtained.

(B) Titanium Compound As the titanium compound, a compound represented by the following general formula (III) can be preferably used from the viewpoint of polymerization activity and the like. _{TiX n (OR) 4-n} ······ (III) [ wherein, X is halogen atom, R represents 1 to carbon atoms
10 hydrocarbon groups, which may be the same or different from each other. n is an integer of 0-4. ]

In the above general formula (III), the halogen atom X is preferably a chlorine atom or a bromine atom, particularly preferably a chlorine atom. As the hydrocarbon group R, an alkyl group, an alkenyl group, a cycloalkenyl group, an aryl group, an aralkyl group and the like are preferable, and a linear or branched alkyl group is particularly preferable. R may be a saturated group or an unsaturated group, may be a linear group, a branched group, or a cyclic group, and further may be sulfur, nitrogen, oxygen, silicon, or phosphorus. Etc. may be included. Specific examples of R include methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group,
sec-butyl group, isobutyl group, n-pentyl group, n
-Hexyl group, n-heptyl group, n-octyl group, n-
Decyl group, allyl group, butenyl group, cyclopentyl group,
Cyclohexyl group, cyclohexenyl group, phenyl group,
Examples thereof include a tolyl group, a benzyl group and a phenethyl group.
Further, n is preferably 4.

Specific examples of the titanium compound (b) represented by the above general formula (III) include tetramethoxytitanium, tetraethoxytitanium, tetra-n-propoxytitanium,
Tetraalkoxytitanium such as tetraisopropoxytitanium, tetra-n-butoxytitanium, tetraisobutoxytitanium, tetracyclohexyloxytitanium and tetraphenoxytitanium; titanium tetrahalide, titanium tetrabromide, titanium tetraiodide and the like. Methoxytitanium trichloride, ethoxytitanium trichloride, propoxytitanium trichloride, n-butoxytitanium trichloride, ethoxytitanium tribromide and other trihalogenated alkoxytitanium; dimethoxytitanium dichloride, diethoxytitanium dichloride, diisopropoxytitanium dichloride, Dihalogenated dialkoxy titanium such as di-n-propoxy titanium dichloride and diethoxy titanium dibromide; trimethoxy titanium chloride, triethoxy titanium chloride, triiso Ropo alkoxy titanium chloride, tri -
Examples include monohalogenated trialkoxy titanium such as n-propoxy titanium chloride and tri-n-butoxy titanium chloride. Of these, titanium compounds having a high halogen content, particularly titanium tetrachloride, are preferred from the viewpoint of polymerization activity. These titanium compounds (b) may be used alone or in combination of two or more.

(C) Halogen compound A halogen compound (c) is optionally used in the solid catalyst component for olefin polymerization. Halogen compound (c)
It is preferable to use since it may improve the particle shape of the olefin polymer or narrow the particle size distribution. Examples of such a halogen compound (c) include halogens such as iodine, bromine, chlorine and fluorine; hydrogen halides such as hydrogen iodide, hydrogen bromide, hydrogen chloride and hydrogen fluoride; silicon tetrachloride and silicon tetrabromide. Silicon halides such as trichlorosilane, dichlorosilane and chlorosilane; carbon halides such as carbon tetrachloride and hexachloroethane;
Halogen-substituted alcohols such as 2,2-trichloroethanol; Halogen-substituted phenols such as p-chlorophenol; Boron halides such as boron trichloride; Aluminum halides such as aluminum trichloride; Tin halides such as tin tetrachloride; Can be mentioned. Among these, silicon tetrachloride is particularly preferable in that a polymer having a better particle shape and a narrower particle size distribution can be obtained. Each of these halogen compounds (c) may be used alone, or
You may use it in combination of 2 or more type.

(D) Electron-donating compound The electron-donating compound (d) is optionally used in the solid catalyst component for olefin polymerization. It is preferable to use the electron-donating compound (d) because the stereoregularity of the olefin polymer may be improved. Examples of the electron-donating compound (d) include alcohols, phenols, ketones, aldehydes, carboxylic acids, malonic acids, esters of organic acids and inorganic acids, ethers such as monoethers, diethers or polyethers. Examples thereof include oxygen-containing compounds and nitrogen-containing compounds such as ammonia, amines, nitriles and isocyanates. Among these, polycarboxylic acid esters are preferable, aromatic polycarboxylic acid esters are more preferable, and aromatic dicarboxylic acid monoesters and / or diesters are particularly preferable from the viewpoint of polymerization activity. The organic group of these ester moieties is preferably a linear, branched or cyclic aliphatic hydrocarbon group.

Specifically, phthalic acid, naphthalene-1,
2-dicarboxylic acid, naphthalene-2,3-dicarboxylic acid, 5,6,7,8-tetrahydronaphthalene-1,2
-Methyl, ethyl, n- of dicarboxylic acids such as dicarboxylic acid, 5,6,7,8-tetrahydronaphthalene-2,3-dicarboxylic acid, indane-4,5-dicarboxylic acid and indane-5,6-dicarboxylic acid Propyl, isopropyl, n-butyl, isobutyl, t-butyl, n-pentyl, 1-methylbutyl, 2-methylbutyl, 3-methylbutyl, 1,1-dimethylpropyl, 1-methylpentyl, 2-methylpentyl, 3-methyl Pentyl, 4-methylpentyl, 1-ethylbutyl, 2-ethylbutyl,
n-hexyl, cyclohexyl, n-heptyl, n-octyl, n-nonyl, 2-methylhexyl, 3-methylhexyl, 4-methylhexyl, 2-ethylhexyl,
3-ethylhexyl, 4-ethylhexyl, 2-methylpentyl, 3-methylpentyl, 2-ethylpentyl,
Examples include dialkyl esters such as 3-ethylpentyl. Among these, the organic group in the ester part has 4 carbon atoms.
The above-mentioned phthalic acid diesters which are linear or branched aliphatic hydrocarbon groups are preferable. Preferred specific examples include di-n-butyl phthalate, diisobutyl phthalate,
Examples thereof include di-n-heptyl phthalate and diethyl phthalate. These electron donating compounds (d) may be used alone or in combination of two or more kinds.

[B] Organoaluminum Compound The organoaluminum compound [B] used in the present invention is not particularly limited, but those having an alkyl group, a halogen atom, a hydrogen atom or an alkoxy group, aluminoxane and a mixture thereof are preferable. Can be used. Specifically, trialkylaluminums such as trimethylaluminum, triethylaluminum, triisopropylaluminum, triisobutylaluminum and trioctylaluminum; dialkyls such as diethylaluminum monochloride, diisopropylaluminum monochloride, diisobutylaluminum monochloride and dioctylaluminum monochloride. Examples include aluminum monochloride; alkylaluminum sesquihalides such as ethylaluminum sesquichloride; and chain aluminoxanes such as methylaluminoxane. Among these, trialkyl aluminum having a lower alkyl group having 1 to 5 carbon atoms, particularly trimethyl aluminum, triethyl aluminum, tripropyl aluminum and triisobutyl aluminum are preferable. These organoaluminum compounds [B] may be used alone or in combination of two or more.

[C] Electron-Donating Compound The electron-donating compound [C] is used for the olefin polymerization catalyst, if necessary. It is preferable to use the electron-donating compound [C] because the stereoregularity of the olefin polymer may be improved. As the electron-donating compound [C], an organosilicon compound having an alkoxy group, a nitrogen-containing compound, a phosphorus-containing compound and an oxygen-containing compound can be used. Among these, it is particularly preferable to use an organosilicon compound having an alkoxy group.

Specific examples of the organosilicon compound having an alkoxy group include trimethylmethoxysilane, trimethylethoxysilane, triethylmethoxysilane, triethylethoxysilane, dimethyldimethoxysilane, dimethyldiethoxysilane, ethylisopropyldimethoxysilane and propylisopropyldimethoxysilane. , Diisopropyldimethoxysilane, diisobutyldimethoxysilane, isopropylisobutyldimethoxysilane, di-t-butyldimethoxysilane, t-butylmethyldimethoxysilane, t-butylethyldimethoxysilane, t
-Butylpropyldimethoxysilane, t-butylisopropyldimethoxysilane, t-butylbutyldimethoxysilane, t-butylisobutyldimethoxysilane, t-
Butyl (s-butyl) dimethoxysilane, t-butylamyldimethoxysilane, t-butylhexyldimethoxysilane, t-butylheptyldimethoxysilane, t-butyloctyldimethoxysilane, t-butylnonyldimethoxysilane, t-butyldecyldimethoxysilane , T
-Butyl (3,3,3-trifluoromethylpropyl)
Dimethoxysilane, cyclohexylmethyldimethoxysilane, cyclohexylethyldimethoxysilane, cyclohexylpropyldimethoxysilane, cyclohexylisobutyldimethoxysilane, dimethoxysilane, dicyclohexyldimethoxysilane, cyclohexyl-t-butyldimethoxysilane, cyclopentylmethyldimethoxysilane, cyclopentylethyldimethoxysilane, cyclopentylpropyl Dimethoxysilane, cyclopentyl-t-butyldimethoxysilane, dicyclopentyldimethoxysilane, cyclopentylcyclohexyldimethoxysilane, bis (2-methylcyclopentyl) dimethoxysilane, bis (2,3-dimethylcyclopentyl)
Dimethoxysilane, α-naphthyl-1,1,2-trimethylpropyldimethoxysilane, n-tetradecanyl-
1,1,2-trimethylpropyl dimethylsilane, 1,
1,2-trimethylpropylmethyldimethoxysilane,
1,1,2-trimethylpropylethyldimethoxysilane, 1,1,2-trimethylpropylisopropyldimethoxysilane, 1,1,2-trimethylpropylcyclopentyldimethoxysilane, 1,1,2-trimethylpropylcyclohexyldimethoxysilane, 1, 1,2-
Trimethylpropylmyristyldimethoxysilane, diphenyldimethoxysilane, diphenyldiethoxysilane, phenyltriethoxysilane, methyltrimethoxysilane, methyltriethoxysilane, ethyltrimethoxysilane, ethyltriethoxysilane, propyltrimethoxysilane, isopropyltrimethoxysilane, Butyltrimethoxysilane, butyltriethoxysilane, isobutyltrimethoxysilane, t-butyltrimethoxysilane, s-butyltrimethoxysilane, amyltrimethoxysilane, isoamyltrimethoxysilane, cyclopentyltrimethoxysilane, cyclohexyltrimethoxysilane, norbornane Trimethoxysilane, indenyltrimethoxysilane, 2-methylcyclopentyltrimethoxysilane, Tilt Li tetraisopropoxysilane,
Methylcyclopentyl (t-butoxy) dimethoxysilane, isopropyl (t-butoxy) dimethoxysilane,
t-butyl (t-butoxy) dimethoxysilane, (isobutoxy) dimethoxysilane, t-butyl (t-butoxy) dimethoxysilane, vinyltriethoxysilane, vinyltributoxysilane, chlorotriethoxysilane,
γ-chloropropyltrimethoxysilane, γ-aminopropyltriethoxysilane, 1,1,2-trimethylpropyltrimethoxysilane, 1,1,2-trimethylpropylisopropoxydimethoxysilane, 1,1,2-
Trimethylpropyl (t-butoxy) dimethoxysilane, tetramethoxysilane, tetraethoxysilane, tetrabutoxysilane, tetraisobutoxysilane, ethyl silicate, butyl silicate, trimethylphenoxysilane, methyltriaryloxysilane, vinyl tris (β-
Examples include methoxyethoxy) silane, vinyltrisacetoxysilane, and dimethyltetraethoxydisiloxane. Of these, dicyclopentyldimethoxysilane,
Cyclohexylisobutyldimethoxysilane and cyclohexylmethyldimethoxysilane are preferred.

As such an organosilicon compound, a silicon compound having no Si--O--C bond and an O--C compound can be used.
A compound obtained by previously reacting an organic compound having a bond or by reacting it at the time of polymerization of α-olefin can also be mentioned. Specific examples include compounds obtained by reacting silicon tetrachloride with alcohol.

Specific examples of the nitrogen-containing compound include 2,6
-Diisopropylpiperidine, 2,6-diisopropyl-4-methylpiperidine, N-methyl-2,2,6,6
-2,6-Substituted piperidines such as tetramethylpiperidine; 2,5-diisopropylazolidine, N-methyl-
2,2,5,5-Tetramethylazolidine and other 2,5-
Substituted azolidines; Substituted methylenediamines such as N, N, N ', N'-tetramethylmethylenediamine, N, N, N', N'-tetraethylmethylenediamine; 1,3
-Dibenzyl imidazolidine, 1,3-dibenzyl-2
-Substituted imidazolidines such as phenylimidazolidine and the like can be mentioned.

Specific examples of the phosphorus-containing compound include triethyl phosphite, tri n-propyl phosphite, triisopropyl phosphite, tri n-butyl phosphite, triisobutyl phosphite, diethyl n-butyl phosphite, diethyl phenyl phosphite. Examples include phosphite esters such as fight.

Specific examples of the oxygen-containing compound include 2,
2,5,5-tetramethyltetrahydrofuran, 2,
2,5,5-tetraethyltetrahydrofuran, etc.
5-Substituted tetrahydrofurans; 1,1-dimethoxy-
2,3,4,5-tetrachlorocyclopentadiene,
Examples include dimethoxymethane derivatives such as 9,9-dimethoxyfluorene and diphenyldimethoxymethane. These electron-donating compounds [C] may be used alone or in combination of two or more.

2. [A] Method for preparing solid catalyst component As a method for preparing the solid catalyst component [A], for example, the above-mentioned magnesium compound (a), titanium compound (b), and if necessary, halogen compound (c) and / or electron. After contacting and reacting the donating compound (d) and, preferably (one or more times), the titanium compound (b) is contacted and reacted again. When the titanium compound (b) is contacted twice or more, the titanium compound (b) can be sufficiently supported on the magnesium compound (a) which functions as a catalyst carrier. Other contact order is not particularly limited.

Each of these components may be contacted in the presence of an inert solvent such as hydrocarbon, or may be diluted with an inert solvent such as hydrocarbon in advance and contacted. Examples of the inert solvent include n-pentane, isopentane,
Examples thereof include aliphatic hydrocarbons such as n-hexane, n-heptane, n-octane and isooctane; aromatic hydrocarbons such as benzene, toluene and xylene, or a mixture thereof. Of these, aliphatic hydrocarbons are preferably used.

The titanium compound (b) is usually 0.5 with respect to 1 mol of magnesium of the magnesium compound (a).
~ 100 mol, preferably 1-50 mol is used.
If it is less than 0.5 mol, the polymerization activity per titanium may decrease. On the other hand, if it exceeds 100 moles, the polymerization activity per solid catalyst component may decrease.

When the halogen compound (c) is used,
Usually, 0.5 to 100 mol is used with respect to 1 mol of magnesium of the magnesium compound (a). If it is less than 0.5 mol, the polymerization activity per titanium and the stereoregularity of the polymer may be lowered. On the other hand, if it exceeds 100 moles, the polymerization activity per solid catalyst component may decrease.

When the electron-donating compound (d) is used, it is generally 0.01 to 10 mol, preferably 0.1 to 1 mol of magnesium of the magnesium compound (a).
05 to 0.15 mol is used. If it is less than 0.01 mol,
The stereoregularity of the polymer may decrease. On the other hand, 1
If it exceeds 0 mol, the polymerization activity per solid catalyst component may decrease.

The contact temperature of these compounds is usually -2.
The temperature may be 0 to 200 ° C., preferably 20 to 150 ° C. The contact time is usually 1 minute to 24 hours, preferably 10 minutes to 6 hours. Outside this range,
It may affect the polymerization activity, stereoregularity, and morphology of the polymer powder. When a solvent is used, the pressure at this time varies depending on its type, contact temperature, etc., but is usually 0 to 5 MPa, preferably 0 to 1 MPa.
In the range of. Further, during the contact operation, it is preferable to perform stirring from the viewpoint of contact uniformity and contact efficiency. These contact conditions are the same for the second and subsequent contact reactions of the titanium compound (b).

In the contact operation of the titanium compound (b),
When a solvent is used, the solvent is usually used in an amount of 5,000 ml or less, preferably 10 to 1,000 ml, based on 1 mol of the titanium compound (b).
If this ratio deviates from the above range, contact uniformity and contact efficiency may be deteriorated.

Further, after the first contact and reaction of each compound, it is usually 90 to 150 ° C., preferably 120 to 140.
Wash with an inert solvent at a temperature of ° C. If the washing temperature is out of the above range, the effect of improving the catalytic activity and stereoregularity may not be sufficiently exhibited. As the inert solvent, the same aliphatic hydrocarbons and aromatic hydrocarbons as described above can be used.

The washing temperature after the second contact with the halogen-containing titanium compound (a) after the second reaction is not particularly limited, but usually 90 to 150 from the viewpoint of stereoregularity.
It may be better to wash with an inert solvent at a temperature of 120C, preferably 120-140C.

The washing method is not particularly limited, but decantation, filtration and the like are preferable. The amount of the inert solvent used, the washing time, and the number of washings are not particularly limited, but are usually 100 to 100,000 ml, preferably 1,000 to 50,000, per 1 mol of the magnesium compound (a). Using a milliliter of solvent, usually 1 minute to 24 hours, preferably 10 minutes to 6
Done on time. If this ratio deviates from the above range, cleaning may be incomplete.

The pressure at this time varies depending on the type of solvent, the washing temperature, etc., but is usually 0 to 5 MPa, preferably 0 to 1 MPa. Also, during the cleaning operation,
It is preferable to perform stirring from the viewpoints of uniformity of cleaning and cleaning efficiency. The obtained solid catalyst component [A] can be stored in a dry state or in an inert solvent such as hydrocarbon.

3. Method for Producing Olefin Polymer The amount of each component of the catalyst for olefin polymerization of the present invention is not particularly limited, but the solid catalyst component [A] is usually converted into titanium atom per 1 liter of reaction volume and ,
The amount used is in the range of 0.00005 to 1 mmol.

The organoaluminum compound [B] has an aluminum / titanium (atomic ratio) of usually 1 to 1,000,
The amount used is preferably in the range of 10 to 1,000. If the atomic ratio deviates from this range, the catalytic activity may be insufficient.

When the electron donating compound [C] is used, the [C] / [B] (molar ratio) is usually 0.001.
To 5.0, preferably 0.01 to 2.0, and more preferably 0.05 to 1.0. If the molar ratio deviates from this range, sufficient catalytic activity and stereoregularity may not be obtained. However, when performing prepolymerization, the amount of the electron-donating compound [C] used can be further reduced.

As the olefin used in the present invention,
Α-Olephy represented by the following general formula (IV) is preferable. _{^{R 1 -CH = CH 2 ··· (}} IV)

In the above general formula (IV), R ¹ is a hydrogen atom or a hydrocarbon group, and the hydrocarbon group may be a saturated group or an unsaturated group, a linear group or a branched group. It may have a chain or may be cyclic. Specifically, ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-
Decene, 3-methyl-1-pentene, 4-methyl-1-
Pentene, vinylcyclohexane, butadiene, isoprene, piperylene and the like can be mentioned. These olefins may be used alone or in combination of two or more. Among these olefins, ethylene and propylene are particularly preferable.

In the polymerization of the olefin in the present invention, the olefin may be prepolymerized first, and then the main polymerization may be carried out, if desired, in view of the polymerization activity, the stereoregularity of the polymer and the powder form. . In this case, the olefin is usually added in the presence of a catalyst prepared by mixing the solid catalyst component [A], the organoaluminum compound [B], and optionally the electron donating compound [C] at a predetermined ratio. At a temperature in the range of 0 to 100 ° C, atmospheric pressure to 5MP
Prepolymerization is carried out at a pressure of about a, and then olefin is main polymerized in the presence of a catalyst and a prepolymerized product.

The type of polymerization in this main polymerization is not particularly limited, and it can be applied to any of solution polymerization, slurry polymerization, gas phase polymerization, bulk polymerization, and the like, and further to both batch polymerization and continuous polymerization. Applicable to two-step polymerization and multi-step polymerization under different conditions.

Regarding the reaction conditions, the polymerization pressure is not particularly limited, and from the viewpoint of polymerization activity, it is usually atmospheric pressure to 8 MPa, preferably 0.2 to 5 MPa, and the polymerization temperature is usually 0 to 200. ° C, preferably 30-100 ° C
Is appropriately selected within the range. The polymerization time is usually 5 minutes to 20 hours, preferably 10 minutes to 10 hours, although it depends on the kind of the olefin as a raw material and the polymerization temperature.

The molecular weight of the olefin polymer can be adjusted by adding a chain transfer agent, preferably hydrogen. Further, an inert gas such as nitrogen may be present. Regarding the catalyst component in the present invention, the solid catalyst component [A], the organoaluminum compound [B] and the electron donating compound [C] are mixed at a predetermined ratio and contacted, and then the olefin is immediately introduced. Polymerization may be performed, or after contacting, aging may be performed for about 0.2 to 3 hours, and then olefin may be introduced to perform polymerization. Furthermore, this catalyst component can be supplied by suspending it in an inert solvent, an olefin or the like. In the present invention, post-treatment after polymerization can be carried out by a conventional method. That is, in the gas phase polymerization method, after the polymerization, the polymer powder discharged from the polymerization vessel may be passed through a nitrogen stream or the like in order to remove olefins and the like contained therein. Depending on the case, it may be pelletized by an extruder, and in that case, a small amount of water, alcohol or the like may be added in order to completely deactivate the catalyst. Further, in the bulk polymerization method, after the polymerization, the monomer can be completely separated from the polymer discharged from the polymerization vessel, and then pelletized.

[0064]

EXAMPLES Next, the present invention will be illustrated concretely by examples, but the present invention is not limited to the following examples.
The average particle size of metallic magnesium (D ₅₀ ); particle size distribution index (P) and sphericity (S) of magnesium compound;
The particle size distribution index (P ') and sphericity (S') of the polymer powder; the stereoregularity [mmmm] of the polymer were determined as follows.

(1) Average particle size of metallic magnesium (D
₅₀ ): The particle size distribution measured using a sieve is plotted on a log-normal probability paper, and the 50% particle size is the average particle size (D ₅₀ ).
Sought as.

(2) Particle size distribution index (P) of magnesium compound: The particle size of the magnesium compound is measured by a light transmission method in a state of being suspended in a hydrocarbon, and the particle size distribution is calculated by a logarithmic normal probability. Plotted on paper, the 50% particle size was taken as the average particle size (D ₅₀ ), and the 90% particle size (D ₉₀ ) and 1
The 0% particle diameter (D ₁₀ ) was obtained and calculated from the above formula (I).

(3) Sphericity (S) of magnesium compound: The magnesium compound after drying was photographed with a scanning electron microscope (JSM-25SIII manufactured by JEOL Ltd.) at an accelerating voltage of 5 KV and 300 times, and a negative image was obtained. Got Next, this negative was image-processed by the transmission method. The image processing is performed by an image analyzer (manufactured by nexsus) to cut particles of 20 pixels (1 pixel is 0.695 μm × 0.695 μm) or less and about 2000 particles remaining,
The longest diameter L ₁ in the projected view of the particles and the diameter L ₂ of the circle equal to the projected area were obtained and calculated by the above formula (II).

(4) Particle size distribution index (P ') of polymerized powder: The particle size distribution measured using a sieve was plotted on a log-normal probability paper, and the 50% particle size was taken as the average particle size (D ₅₀ ). The 90% particle diameter (D ₉₀ ) and the 10% particle diameter (D ₁₀ ) were obtained and calculated from the above formula (I).

(5) Sphericity (S ') of polymerized powder: A polyolefin powder photographed with a polarizing microscope (BHS-751P manufactured by OLYMPUS) at 40 times was subjected to image processing. For image processing, 1 pixel is 10.4 μm × 10.4
μm, and was calculated in the same manner as the magnesium compound except that about 300 particles were analyzed.

(6) Stereoregularity of polymer [mmmm]:
Dissolve the polymer in 1,2,4-trichlorobenzene,
¹³ C-NMR (manufactured by JEOL Ltd., trade name: EX-4
00) was used to quantify using the signal of the methyl group measured by the complete proton decoupling method at 130 ° C.

The isotactic pentad fraction [m
mmm] means A. Zambell
i) etc. are Macromolecules (Macromole
Cules) Vol. 6, page 925 (1973), means the isotactic fraction in the pentad unit in the polypropylene molecular chain, which is determined from the ¹³ C-NMR spectrum. The method for determining the attribution of ¹³ C-NMR spectrum peaks is described in A. Zamberg (A. Zam).
belli) and other macromolecules (Macro)
Volumes) Vol. 8, page 687 (1975)
I followed the attribution proposed in.

Example 1 (1) Preparation of Magnesium Compound Agitator equipped with four baffles (max blend impeller, impeller diameter d = 0.09) with an internal volume of 5 liters, which was replaced with nitrogen.
m) In a three-necked flask equipped with
274 g (49 gram atom), 12 g of iodine (95 milligram atom), and 120 g (4.9 gram atom) of metal magnesium (cut and crushed product) having an average particle diameter (D ₅₀ ) of 400 μm (ethanol / metal magnesium ( ROH / Mg) (molar ratio) = 10). These are stirred at 78 ° C. until hydrogen is no longer generated from the system (stirring number n
= 250 (times / minute) (hereinafter referred to as rpm), n ³ d ²
= 1.27 × 10 ⁵ ) and reacted to obtain a magnesium compound (dietomagnesium). The results are shown in Table 1.

(2) Preparation of solid catalyst component In a three-necked flask equipped with a stirrer and having an internal volume of 0.5 liter, which was purged with nitrogen, 16 g of the magnesium compound (support) prepared in the above (1) and octane 80 dehydrated Added milliliters. This was heated to 40 ° C., 2.4 ml (23 mmol) of silicon tetrachloride was added and stirred for 20 minutes, and then 3.4 ml (13 mmol) of di-n-butyl phthalate was added. The temperature of this solution was raised to 80 ° C., and subsequently, using a dropping funnel, titanium tetrachloride 7 was added.
7 ml (0.70 mol) was added dropwise, and the internal temperature was 125.
Stirring was carried out at 0 ° C. for 1 hour to carry out a supporting operation. Then, it was thoroughly washed with dehydrated octane. After that, 122 ml of titanium tetrachloride (1.11 mol) was added,
The mixture was stirred at an inner temperature of 125 ° C. for 2 hours, and the second loading operation was performed. Then, it was sufficiently washed with dehydrated octane to obtain a solid catalyst component.

(3) Propylene Slurry Polymerization A stainless steel autoclave with an internal volume of 1 liter equipped with a stirrer was thoroughly dried and replaced with nitrogen, and then 500 ml of dehydrated heptane was added. To this, 2.0 mmol of triethylaluminum, 0.25 mmol of dicyclopentyldimethoxysilane, and 0.0025 mmol in terms of Ti atom of the solid catalyst component prepared in (2) above were added,
Hydrogen was injected into the autoclave at a pressure of 0.1 MPa, and then, while introducing propylene, the temperature was raised to 80 ° C. and the total pressure was increased to 0.8 MPa, and then polymerization was performed for 1 hour. Then, the temperature was lowered and the pressure was released, and the contents were taken out and put into 2 liters of methanol to deactivate the catalyst. It was filtered off and dried in vacuum to obtain a propylene polymer (polypropylene). The results are shown in Table 1.

Example 2 (1) Preparation of magnesium compound In Example 1 (1), the amount of iodine used was 3.6 g.
(28 mg atom), the reaction temperature was 50 ° C., the stirring number (n) was 375 rpm (n ³ d ² = 4.27 × 1).
A magnesium compound was obtained in the same manner as in Example 1 (1), except that the magnesium compound was 0 ⁵ ). The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Example 3 (1) Preparation of Magnesium Compound In Example 1 (1), 1.5 g (31 mg atom) of anhydrous magnesium chloride was used in place of iodine, and 40 g (1.6 g) of magnesium metal was used. atom),
A magnesium compound was obtained in the same manner as in Example 1 (1) except that ROH / Mg = 30. The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Example 4 (1) Preparation of magnesium compound In Example 1 (1), the average particle diameter (D ₅₀ ) was 75.
Using metal magnesium (cut and crushed product) of μm, ethanol / metal magnesium (molar ratio) was 8, stirring number (n) was 150 rpm (n ³ d ² = 2.73 × 10 ⁴ ).
A magnesium compound was obtained in the same manner as in Example 1 (1) except that The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Example 5 (1) Preparation of magnesium compound In Example 4 (1), the average particle size (D ₅₀ ) was 18
Using metallic metal (cut and crushed) of 00 μm,
The stirring number (n) was set to 400 rpm (n ³ d ² = 5.18 × 1).
A magnesium compound was obtained in the same manner as in Example 4 (1) except that the compound was changed to 0 ⁵ ). The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 1 (1) Preparation of Magnesium Compound In Example 4 (1), the average particle size (D ₅₀ ) was 24.
Using metallic metal (cut and crushed) of 00 μm,
Stirring number (n) is 250 rpm (n ³ d ² = 1.27 × 1)
A magnesium compound was obtained in the same manner as in Example 4 (1) except that the compound was changed to 0 ⁵ ). The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 2 (1) Preparation of Magnesium Compound In Example 2 (1), the average particle diameter (D ₅₀ ) was 40.
Using metallic magnesium (cut and crushed product) of μm, the amount of iodine used was 3.6 g (28 mg atom), and the stirring number (n) was 200 rpm (n ³ d ² = 6.48 × 10).
^A magnesium compound was obtained in the same manner as in Example 1 (1) except that the above was adopted. The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 3 (1) Preparation of Magnesium Compound A magnesium compound was obtained in the same manner as in Example 1 (1) except that ethanol / metal magnesium (molar ratio) was changed to 50 in Example 1 (1). It was The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 4 (1) Preparation of Magnesium Compound A magnesium compound was obtained in the same manner as in Example 1 (1) except that ethanol / metal magnesium (molar ratio) was changed to 3. It was The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 5 (1) Preparation of Magnesium Compound In Example 4 (1), the average particle diameter (D ₅₀ ) was 60.
Using 0 μm metallic magnesium (cut and crushed product), stirring number (n) was 60 rpm (n ³ d ² = 1.75 × 1)
A magnesium compound was obtained in the same manner as in Example 4 (1) except that the compound was changed to 0 ⁵ ). The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

Comparative Example 6 (1) Preparation of Magnesium Compound In Example 4 (1), the average particle size (D ₅₀ ) was 20.
Using 0 μm metallic magnesium (cut and crushed product), stirring number (n) was 800 rpm (n ³ d ² = 4.15 × 10).
^A magnesium compound was obtained in the same manner as in Example 4 (1) except that the above was adopted. The results are shown in Table 1. (2) Preparation of solid catalyst component A solid catalyst component was prepared in the same manner as in Example 1 (2) except that the magnesium compound prepared in (1) above was used in Example 1 (2). (3) Propylene Slurry Polymerization Propylene was polymerized in the same manner as in Example 1 (3) except that the solid catalyst component prepared in (2) above was used in Example 1 (3). The results are shown in Table 1.

[0085]

[Table 1]

[0086]

According to the present invention, the particle size distribution is narrow without deteriorating the catalytic performance such as stereoregularity and polymerization activity.
It is possible to provide a magnesium compound that gives an olefin polymer having a nearly spherical shape, a solid catalyst component for olefin polymerization, a catalyst for olefin polymerization, and a method for producing polyolefin.

[Brief description of drawings]

FIG. 1 is a schematic diagram showing a method for producing an olefin polymerization catalyst of the present invention.

   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Masahiko Kuramoto             1 Iezaki coast, Ichihara city, Chiba prefecture F-term (reference) 4H006 AA01 AA02 AB40 AC90 BC18                       BC31 BE24 BE53 FE11                 4H048 AA01 AA02 AB40 AC90 BE21                       BE53 VA20 VA60 VB10                 4J128 AA01 AB01 AC04 AC05 AC06                       AC07 BA01B BB01B BC14B                       BC15B BC16B BC25B CB22A                       CB22C CB27A CB27C CB36A                       CB52A CB52C CB53A CB53C                       CB54A CB54C CB62A CB62C                       CB65A CB65C CB68A CB68C                       CB79A CB79C EB01 EB02                       EB03 EB04 EB05 EB07 EB08                       EB09 EB13 EB14 FA01 FA02                       FA03 FA04 GA12 GA26 GB01                       GB02

Claims (11)

[Claims] 1. A metal magnesium having an average particle diameter (D ₅₀ ) of ₅₀ to 2000 μm corresponding to a cumulative weight fraction of 50%, and a molar ratio (ROH /
(Mg) alcohol having 4 to 40, and halogen and / or a halogen-containing compound containing 0.0001 gram atom or more of a halogen atom with respect to 1 gram atom of the metal magnesium are provided in a stirring blade having a blade diameter d (m). When stirring and reacting in a stirring tank having a stirring shaft provided at a rotation speed n (times / minute), n ³ d ² is adjusted to 4.3 × 10 ^{3 to} 4.0 × 10 ^6. A magnesium compound obtained by stirring and reacting. 2. The magnesium compound according to claim 1, wherein the halogen is iodine. 3. The magnesium compound according to claim 1, wherein the halogen-containing compound is magnesium chloride. 4. The magnesium compound according to claim 1, wherein the reaction temperature of the metal magnesium, the alcohol, and the halogen and / or the halogen-containing compound is 30 to 90 ° C. 5. The particle size distribution index (P) represented by the following formula (I) is less than 3.4, and the sphericity (S) represented by the following formula (II) is less than 1.30. The magnesium compound according to any one of claims 1 to 4. P = (D ₉₀ / D ₁₀ ) ... (I) [wherein, D ₉₀ is the particle diameter of the magnesium compound corresponding to a cumulative weight fraction of 90%, and D ₁₀ is a cumulative weight. The particle diameter of the magnesium compound corresponding to a fraction of 10% is shown. ] S = (L ₁ / L ₂ ) ³ (II) [wherein, L ₁ is the longest diameter of the projected view of the magnesium compound obtained by scanning with an electron microscope and image processing. And L ₂ represents the diameter of a circle equal to the projected area of the magnesium compound. ] 6. A solid catalyst component for olefin polymerization obtained by reacting (a) the magnesium compound according to any one of claims 1 to 5 and (b) a titanium compound. 7. The solid catalyst component for olefin polymerization according to claim 6, which further comprises reacting (c) a halogen compound and / or (d) an electron donating compound. 8. The solid catalyst component for olefin polymerization according to claim 7, wherein the halogen compound (c) is silicon tetrachloride. 9. An olefin polymerization catalyst comprising the following compounds [A] and [B] or the following compounds [A], [B] and [C]. [A] The solid catalyst component [B] organoaluminum compound [C] electron-donating compound for olefin polymerization according to any one of claims 6 to 8. 10. A method for producing a polyolefin using the catalyst for olefin polymerization according to claim 9. 11. Metal magnesium having an average particle diameter (D ₅₀ ) corresponding to a cumulative weight fraction of 50% of ₅₀ to 2000 μm, and a molar ratio (ROH /
(Mg) alcohol having 4 to 40, and halogen and / or a halogen-containing compound containing 0.0001 gram atom or more of halogen atom per 1 gram atom of the metal magnesium are provided in a stirring blade having a blade diameter d (m). When stirring and reacting in a stirring tank having a stirring shaft provided at a rotation speed n (times / minute), n ³ d ² is adjusted to 4.3 × 10 ^{3 to} 4.0 × 10 ^6. A method for producing a magnesium compound which is reacted by stirring.