JPS646645B2 - - Google Patents

Description

[Detailed description of the invention]

The present invention relates to a method for polymerizing α-olefins. A method of polymerizing an α-olefin having 3 or more carbon atoms in the presence of a solid catalyst component in which a titanium halide is supported on a magnesium compound, an organoaluminum compound, and an aromatic carboxylic acid ester is known. According to this method,
This is an excellent method in that α-olefin polymers with high stereoregularity can be obtained in extremely high yields, so that the operation for removing residual catalyst residues from the produced α-olefin polymers is not necessary or can be significantly simplified. effect is achieved. However, the α-olefin polymer obtained by this method generates an odor due to compounds attributable to the aromatic carboxylic acid ester added to the polymerization system. In particular, when the above polymer is molded, a strong odor is generated and the working environment is significantly polluted, which is a major obstacle to the industrial implementation of the above method. As a method for removing this odor, a method has been proposed in which the above polymer is treated with steam (Japanese Patent Application Laid-Open No. 1986-1999-1).
Publication No. 24407). According to the proposed method, the odor of α-olefin polymer can be almost eliminated, but it requires the use of a large amount of steam;
Furthermore, there is a drawback that a large amount of heat and time are required to dry the polymer after steam treatment. An object of the present invention is to provide a method for polymerizing α-olefin that is odorless and has high stereoregularity and can be obtained in high yield. The purpose of the present invention is to (1) convert aluminum halide into a compound having the formula R ¹ lSi(OR ² ) _4-l [] (wherein R ¹ represents an alkyl group or phenyl group having 1 to 8 carbon atoms, and R ² represents an alkyl group having 1 to 8 carbon atoms, and 1 is 0, 1, 2 or ³ . , R ³ represents an alkyl group having 1 to 8 carbon atoms, and X represents a halogen atom. (2) A solid catalyst component (A) obtained by contacting the contacted solid with titanium tetrahalide, or (b) contacting with a titanium tetrahalide and an aromatic carboxylic acid ester, Organoaluminum compound represented by AlR ⁴ ₃ [] (wherein R ⁴ represents an alkyl group having 2 to 6 carbon atoms)
(B), and the formula R ⁵ mR ⁶ nCH _3-(o+n) OH [] (wherein, R ⁵ represents an alkyl group or phenyl group having 1 to 12 carbon atoms, R ⁶ represents a phenyl group, m is an integer of 0 to 2, and n is an integer of 1 to 3. However, n+m is 3 or less.)
This is achieved by polymerizing an α-olefin having 3 or more carbon atoms in the presence of a catalyst obtained from phenyl carbinols (C) represented by: According to the present invention, odorless α-olefin polymers can be obtained in extremely high yields, so that the excellent effect of omitting the deodorizing operation of the produced polymer and the removal operation of catalyst residues is achieved. In addition, in the present invention, an aromatic carboxylic acid ester is used during the preparation of the solid catalyst component (A), but since only a small amount of this is incorporated into the solid catalyst component (A), it is not included in the produced α-olefin polymer. It does not generate any odor. FIG. 1 shows the method for polymerizing α-olefin of the present invention and the process for preparing the solid catalyst component used in the polymerization. In the present invention, the preparation and polymerization of the solid catalyst component are all carried out under an inert gas atmosphere such as nitrogen or argon. Further, it is desirable that the raw material for preparing the solid catalyst component is substantially anhydrous. The solid catalyst component (A) used in the present invention is:
Japanese Patent Application Laid-Open No. 56-45909 filed by the present applicant,
It can be prepared according to the method described in JP-A-56-163102 and Japanese Patent Application No. 56-140361. Specific examples of aluminum halide in the present invention include aluminum chloride, aluminum bromide, and aluminum iodide, among which aluminum chloride is preferably used. Specific examples of silicon compounds include tetramethoxysilane, tetraethoxysilane, and tetra-n-
Propoxysilane, tetra-n-butoxysilane, tetra-isopentoxysilane, tetra-n
-hexoxysilane, methyltrimethoxysilane, methyltriethoxysilane, methyltri-n
-Butoxysilane, methyltriisopentoxysilane, methyltri-n-hexoxysilane, methyltriisooctoxysilane, ethyltriethoxysilane, ethyltriisopropoxysilane, ethyltriisopentoxysilane, n-butyltriethoxysilane, isobutyl Triethoxysilane, isopentyltriethoxysilane, isopentyltri-n-butoxysilane, dimethyldiethoxysilane, dimethyldi-n-butoxysilane,
Dimethyldiisopentoxysilane, diethyldiethoxysilane, diethyldiisopentoxysilane, di-n-butyldiethoxysilane, diisobutyldiisopentoxysilane, trimethylmethoxysilane, trimethylethoxysilane, trimethylisobutoxysilane, triethyliso Propoxysilane, tri-n-propylethoxysilane,
Tri-n-butylethoxysilane, triisopentylethoxysilane, phenyltriethoxysilane, phenyltriisobutoxysilane, phenyltriisopentoxysilane, diphenyldiethoxysilane, diphenyldiisopentoxysilane,
Examples include diphenyldioctoxysilane, triphenylmethoxysilane, triphenylethoxysilane, and triphenylisopentoxysilane. The proportion of aluminum halide used in the reaction is preferably 0.1 to 10 mol, particularly 0.3 to 2 mol, per mol of silicon compound. The reaction between aluminum halide and a silicon compound is usually carried out by combining both compounds in an inert organic solvent with -
This is carried out by stirring for 0.1 to 2 hours at a temperature in the range of 50 to 100°C. The reaction proceeds with exotherm, and the reaction product is obtained as a solution in an inert organic solvent. Note that when using a tetraalkoxysilane in which l is 0 in the formula [], a small amount of insoluble matter may be produced. Although this insoluble matter does not inhibit the polymerization activity of the ultimately obtained catalyst, it is desirable to separate it from the reaction product mixture in order to facilitate the preparation operation of the solid catalyst component. The reaction product is subjected to the reaction with the Grignard compound as a solution in an inert organic solvent. Among the Grignard compounds represented by the formula [], alkylmagnesium chlorides in which X is a chlorine atom are preferably used, and specific examples thereof include methylmagnesium chloride, ethylmagnesium chloride, n-butylmagnesium chloride, and n-hexylmagnesium chloride. Examples include. The amount of Grignard compound used is preferably 0.05 to 4 mol, especially 1 to 3 mol, per mol of aluminum halide used for the preparation of the reaction product. There is no particular restriction on the method of reacting the reaction product with the Grignard compound, but an ether solution of the Grignard compound or a mixed solvent solution of ether and an aromatic hydrocarbon is gradually added to the solution of the reaction product in an inert organic solvent. Conveniently this is done by addition or addition in the reverse order. As the above-mentioned ether, a compound represented by the formula R ⁷ -O-R ⁸ (in the formula, R ⁷ and R ⁸ represent an alkyl group having 2 to 8 carbon atoms) is preferably used, and specific examples thereof include: , diethyl ether, diisopropyl ether, di-n-butyl ether, diisoamyl ether and the like. The reaction temperature is usually -50 to 100℃, preferably -20℃
~25℃. There is no particular restriction on the reaction time, but it is usually 5 minutes or more. As the reaction progresses, a white carrier precipitates out. Although the carrier thus obtained can be used as a reaction mixture for the next treatment, it is preferable to separate the carrier in advance and wash it with an inert organic solvent before using it for the next treatment. In the present invention, the carrier is then selected from the following (a) or
Contact with titanium tetrahalide and aromatic carboxylic acid ester by method (b). (b) The support is brought into contact with titanium tetrahalide in the presence or absence of an inert organic solvent at a temperature of 20 to 200°C, preferably 60 to 140°C, for 0.5 to 3 hours, and the resulting solid is After separation and washing, an aromatic carboxylic acid ester is added to a suspension of the solid in an inert organic solvent, and the mixture is brought into contact with the suspension at a temperature of 0 to 200°C, preferably 5 to 150°C, for 5 minutes or more. (b) Contacting the support with titanium tetrahalide and aromatic carboxylic acid ester at a temperature of 20 to 200°C, preferably 60 to 140°C, for 0.5 to 3 hours in the presence or absence of an inert organic solvent. How to do it. Specific examples of titanium tetrahalide include titanium tetrachloride, titanium tetrabromide, and titanium tetraiodide, of which titanium tetrachloride is preferably used. The amount of titanium tetrahalide used is 1 mole of Grignard compound used in preparing the carrier.
The amount is preferably 2 to 100 moles or more, particularly 2 to 100 moles. As aromatic carboxylic acid ester, [In the formula, R ⁹ represents an alkyl group having 1 to 6 carbon atoms, and Y represents a hydrogen atom, an alkyl group having 1 to 4 carbon atoms, or -OR ¹⁰ (R ¹⁰ represents an alkyl group having 1 to 4 carbon atoms). ) is shown. ] are preferably used, specific examples of which include methyl benzoate,
Examples include ethyl benzoate, methyl toluate, ethyl toluate, methyl anisate, and ethyl anisate. The contact solid obtained by the method (a) or (b) above,
A solid catalyst component (A) is prepared by contacting it again with titanium tetrahalide. Conditions such as the amount of titanium tetrahalide used, contact temperature, and contact time are the same as those for preparing the contact solid. The solid catalyst component (A) is separated from the thus obtained mixture containing the solid catalyst component (A) by filtration, decanting, etc., and washed with an inert organic solvent. Solid catalyst component (A)
It contains 0.5 to 5% by weight of titanium. In the present invention, the solid catalyst component (A), formula []
In the presence of a catalyst obtained from an organoaluminum compound (B) represented by
Polymerize olefin. Specific examples of organoaluminum compounds (B) include:
Examples include triethylaluminum, triisobutylaluminum, tri-n-hexylaluminum, and the like, among which triethylaluminum and triisobutylaluminum are preferably used. The amount of organoaluminum compound (B) used is usually 1 gram atom of titanium in the solid catalyst component (A).
~1000 mol. Specific examples of phenyl carbinols (C) include:
Examples include dimethylphenyl carbinol, methylphenyl carbinol, ethyl phenyl carbinol, diphenyl carbinol, diethyl phenyl carbinol, triphenyl carbinol, dibutylphenyl carbinol, and dipropylphenyl carbinol. phenyl carbinols
The amount of (C) used is preferably 0.01 to 1 mol, particularly 0.05 to 0.5 mol, per 1 mol of organoaluminum compound (B). Specific examples of α-olefins having 3 or more carbon atoms include propylene, butene-1,4-methylpentene-1, hexene-1, and the like. In the present invention, the α-olefin described above can be used alone or copolymerized, and the α-olefin described above and ethylene can also be copolymerized. The polymerization reaction can be carried out in the same manner as the polymerization reaction of α-olefin using a conventional Ziegler-Natsuta type catalyst. The polymerization reaction can be carried out in liquid phase or gas phase. When the polymerization reaction is carried out in a liquid phase, an inert organic solvent may be used as the polymerization solvent, or the liquid α-olefin itself may be used as the polymerization solvent. There are no particular restrictions on the catalyst concentration in the polymerization solvent, but in general, the solid catalyst component (A) is 0.001 to 1 milligram atom in terms of titanium metal per polymerization solvent, and the organoaluminum compound (B) is
0.01-100 mmol. In this invention, when preparing the solid catalyst component (A),
Examples of the inert organic solvent that may be used in the polymerization reaction include aliphatic hydrocarbons such as hexane and heptane, aromatic hydrocarbons such as toluene, benzene, and xylene, and halides of these hydrocarbons. The polymerization reaction is carried out in the substantial absence of moisture and oxygen. The polymerization temperature is usually 30 to 100°C, and the polymerization pressure is usually 1 to 80 kg/cm ² . The molecular weight of the α-olefin polymer obtained by the method of this invention can be easily adjusted by adding hydrogen to the polymerization system. Next, examples will be shown. In the following description,
"Polymerization activity" refers to the polymer yield per 1 hour of polymerization time per 1 g of solid catalyst component used in the polymerization reaction.
(g), and "HI" refers to the boiling n-
This is the weight percentage of the extraction residue based on the total polymer when extracted with heptane for 20 hours. In the Examples, all solid catalyst components were prepared in a dry nitrogen gas atmosphere. Example 1 (1) Preparation of solid catalyst component Toluene suspension of 2.0 g of anhydrous aluminum chloride 30
ml was added with 10 ml of a toluene solution containing 3.0 ml of methyltriethoxysilane, and the mixture was reacted at 25° C. for 1 hour with stirring.Then, the reaction mixture was heated to 60° C. and reacted at the same temperature for 1 hour. The reaction mixture was cooled to -10°C and a solution of 3.72 g of n-butylmagnesium chloride in 17 ml of diisoamyl ether was added to the reaction mixture over 30 minutes while stirring. The temperature of the reaction system was maintained at -10°C. The temperature of the reaction mixture was raised to 30°C, and the reaction was continued at the same temperature for 1 hour. The precipitated carrier was separated and washed with toluene. Titanium tetrachloride in 25 ml of toluene suspension of 3.4 g of carrier.
10 ml was added and kept at 90°C for 1 hour while stirring. After separation from the mixture at the same temperature, 0.65 ml of ethyl benzoate was added to 25 ml of a toluene suspension of the solid obtained by washing with toluene, and the mixture was maintained at 90° C. for 1 hour with stirring. The resulting contact solid was separated at 90°C and washed with n-heptane and then toluene. Titanium tetrachloride in 30 ml of toluene suspension of the contact solid
10 ml was added and kept at 90°C for 1 hour while stirring. The obtained solid catalyst component was separated at 90°C and washed with n-heptane. 2.7g of solid catalyst component to n-heptane
A solid catalyst component slurry was prepared by suspending the solid catalyst component in 80 ml. The titanium content of the solid catalyst component is 2.83% by weight
It was hot. (2) Polymerization A glass ampoule containing 37.6 mg of solid catalyst component slurry was attached to a separable flask with an internal volume of 500 ml, and then the air in the flask was replaced with nitrogen. Add 300 ml of n-heptane to the flask under a nitrogen gas atmosphere, and while introducing propylene,
The temperature was raised to 60°C. 0.22 mmol of triethylaluminum, then dimethylphenyl carbinol
After adding 0.11 mmol to the flask, stirring was started and the glass ampoule was crushed to initiate atmospheric polymerization of propylene. During polymerization, propylene was continuously supplied at a rate of 1/min, and the polymerization temperature was kept at 60°C.
It was kept at ℃. One hour after the start of polymerization, 100 ml of isopropanol was added to the flask to stop the polymerization. The contents of the flask were poured into isopropanol 0.9 mm, stirred for 30 minutes, and the resulting polymer was heated to 60°C.
Dry under reduced pressure for 20 hours to form powdered polypropylene
Obtained 32.8g. The polymerization activity was 873 and the HI was 95.2%. Examples 2 to 4 In place of dimethylphenyl carbinol, the first
Example 1 was repeated except that 0.11 mmol of the phenyl carbinols listed in the table was used. The results are shown in Table 1.

[Table] Example 5 The amount of dimethylphenyl carbinol used was 0.15
Example 1 was repeated except that millimoles were changed. The polymerization activity was 715 and the HI was 97.1%. Example 6 Example 1 was repeated, except that 34.5 mg of the solid catalyst component (titanium content: 2.91% by weight) slurry obtained by replacing methyltriethoxysilane with 3.4 ml of tetraethoxysilane was used. The polymerization activity was 802 and the HI was 94.3%. Example 7 A glass ampoule containing 10.5 mg of the solid catalyst component slurry prepared in Example 1 was placed in an autoclave with an internal volume of 2 and equipped with a stirrer, and the air in the autoclave was replaced with nitrogen. 5.9 ml of a solution of 1.24 mmol of triethylaluminum in n-heptane, then 4.0 ml of a solution of 0.30 mmol of dimethylphenyl carbinol in n-heptane.
was introduced into the autoclave. liquid propylene
After introducing 1200 ml, the autoclave was shaken and the contents were then heated to 65°C. Stirring was started, the glass ampoule was crushed, and propylene was polymerized at 65° C. for 1 hour. After the polymerization reaction was completed, unreacted propylene was discharged, glass fragments were removed, and the resulting polypropylene was dried under reduced pressure at 50°C for 20 hours. 152 g of polypropylene were obtained. Polymerization activity is
14500, HI was 94.1%. Example 8 Example 1 was repeated except that 10 ml of titanium tetrachloride and 0.65 ml of ethyl benzoate were added to the toluene suspension of the carrier and held at 90° C. for 1 hour to prepare a contact solid. The polymerization activity was 850 and the HI was 95.4%. In addition,
The titanium content of the solid catalyst component was 2.30% by weight. The polypropylenes obtained in Examples 1 to 8 were odorless and did not emit any odor even when heated and melted at 230°C.

[Brief explanation of the drawing]

FIG. 1 is a flowchart showing the method for polymerizing α-olefin of the present invention.

Claims (1)

[Scope of Claims] 1 Aluminum halide has the formula R ¹ lSi(OR ² ) _4-l (wherein R ¹ represents an alkyl group having 1 to 8 carbon atoms or a phenyl group, and R ² represents an alkyl group having 1 to 8 carbon atoms). 8 alkyl group, l is 0, 1, 2 or 3)
2 The reaction product is reacted with a Grignard compound represented by the formula R ³ MgX (wherein R ³ represents an alkyl group having 1 to 8 carbon atoms, and X represents a halogen atom). 3. Contacting the obtained carrier with (a) titanium tetrahalide and then aromatic carboxylic acid ester, or (b) contacting titanium tetrahalide and aromatic carboxylic acid ester, 4. A solid catalyst component (A) obtained by contacting with titanium halide, an organoaluminum compound (B) represented by the formula AlR ⁴ ₃ (in the formula, R ⁴ represents an alkyl group having 2 to 6 carbon atoms), and Formula R ⁵ mR ⁶ nCH _3-(o+n) OH (wherein, R ⁵ represents an alkyl group or phenyl group having 1 to 12 carbon atoms, R ⁶ represents a phenyl group,
m is an integer of 0 to 2, and n is an integer of 1 to 3. However, n+m is 3 or less. 1. A method for polymerizing α-olefin, which comprises polymerizing α-olefin having 3 or more carbon atoms in the presence of a catalyst obtained from phenyl carbinols (C) represented by (C).