JP2715112B2 - Catalyst for polymerization of olefins - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention can provide a highly stereoregular polymer which acts with high activity and is well-shaped when subjected to polymerization of olefins. It relates to a high-performance catalyst. More specifically, the present invention provides a catalyst for polymerization of olefins comprising a special solid catalyst component (I), a specific silicon compound (II) and an organoaluminum compound (III), as described in detail below. It is.

[Conventional technology and its problems]

Recently, titanium catalyst, an active component, is supported on magnesium chloride together with an electron donor as a new type of catalyst component in place of the conventionally known titanium trichloride catalyst component as a solid catalyst component in olefin and other olefin polymerization catalysts. Many things have been developed and proposed.

Of these, the earliest ones were developed by co-milling a complex of an organic monocarboxylic acid ester as an electron donor and titanium tetrachloride with magnesium chloride, or an organic monocarboxylic acid as an electron donor. There is a product obtained by treating a co-ground product of an acid ester and magnesium chloride with titanium tetrachloride.

However, when these are used in combination with an organoaluminum compound to industrially conduct polymerization of olefins, particularly stereoregular polymerization of propylene, 1-butene, etc., an organic monocarboxylic acid is used as an electron donor during the polymerization reaction. It is essential to use an ester, and in this case, it is necessary to use an organic monocarboxylic acid ester in an extremely large amount, so that there is a problem in that a characteristic ester smell is imparted to the produced polymer.

Further, in these catalysts, the activity in the early stage of polymerization is high, but the deactivation with time is large, which causes a problem in the process operation.In addition, when the polymerization time such as block copolymerization is made longer, it is practically not used. It was impossible.

In order to improve this point, Japanese Patent Application Laid-Open No. 54-94590 discloses a method of preparing a catalyst component using a magnesium dihalide as a starting material and preparing an organoaluminum compound, an organic carboxylic acid ester and a compound having a MOR group. A method of combining and using olefins for polymerization is disclosed, but as is clear from the description of the publication, in this case, it is necessary to use an organic carboxylic acid ester both at the time of catalyst preparation and at the time of polymerization. In general, the amount of the organic carboxylic acid ester contained in the catalyst is such that the problem of the odor of the produced polymer can be ignored by treatment with a titanium halide or washing with an organic solvent. However, as described above, the amount of the organic carboxylic acid ester used in the polymerization is extremely large as compared with the amount contained in the catalyst, and when the polymerization is performed in a liquid or gaseous monomer, almost all of the organic carboxylic acid ester is used. At present, it is contained in the produced polymer. Therefore, it can be said that the problem of odor of the produced polymer cannot be solved as long as an organic carboxylic acid ester is used at the time of polymerization. Also, the method disclosed in the publication requires very complicated operations and the obtained catalyst is practically sufficient in terms of performance and sustainability of the activity, as can be seen from the examples. This is not the case.

[Means for solving the problem]

The present inventors have conducted intensive studies to solve the various problems in the prior art as described above. As a result, the present invention provides a high-performance catalyst by which a polymer having a high stereoregularity can be obtained by the present invention. Succeeded.

That is, the present invention provides a catalyst for polymerization of olefins, comprising a solid catalyst component of the following (I), a silicon compound of the following (II), and an organoaluminum compound of the following (III).

(I) After pulverizing the substance (a) and the phthalic acid diester (b) obtained by reacting a metal magnesium powder with two or more moles of an alkyl monohalide in the presence of iodine, a fat is added to the obtained product. In the presence of an aromatic hydrocarbon (c), a tetraalkoxytitanium (d), an aliphatic alcohol (e) and a phthalic acid dichloride (f) are sequentially added at 70 ° C. or higher, and each treatment is carried out. A solid catalyst component obtained by adding titanium chloride (g) and further processing; (II) a general formula SiR _m (OR ′) _4-m (where R is an alkyl group, a cycloalkyl group, a vinyl group or an aryl group) And R ′ is an alkyl group. When R is an alkyl group, the alkyl group may be the same as R ′, and m is 0 ≦ m <4.) And (III) In the general formula RnAlX3-n, R is an alkyl group having 1 to 4 carbon atoms, X is any one of hydrogen, chlorine, bromine and iodine, and n is 0 <n ≦ 3. The present invention provides a catalyst for polymerization of olefins, comprising an organoaluminum compound represented by the formula (hereinafter sometimes simply referred to as “organoaluminum compound”).

Hereinafter, the olefin polymerization catalyst of the present invention will be described in more detail.

 First, the solid catalyst component (I) will be described.

In order to obtain a substance (hereinafter simply referred to as a substance (a)) obtained by reacting the above-mentioned (a) metal magnesium powder with an alkyl monohalide in the presence of iodine, a commercially available metal magnesium powder and an alkyl monohalide may be used. The halide is reacted with the halide in the absence of an organic solvent in the presence of iodine. In this case, it is necessary to use 2 mol or more of the alkyl monohalide per 1 mol of the metal magnesium powder. The reaction temperature and the reaction time are optional as long as the above reaction sufficiently proceeds, and are not particularly limited.
Performed for at least 30 minutes. This reaction is a Grignard type reaction. When the IR spectrum of the substance (a) obtained by the reaction is measured, absorption of an alkyl group is observed.

As the alkyl monohalide used in the production of the above (a) substance, a chloride of an aliphatic hydrocarbon which is liquid at normal temperature is preferable, and examples thereof include n-propyl chloride, isopropyl chloride, n-butyl chloride, and the like. Isobutyl chloride, pentyl chloride, hexyl chloride, octyl chloride and the like.

Examples of the phthalic acid diester (b) (hereinafter simply referred to as (b) substance) include dimethyl phthalate, diethyl phthalate, diisopropyl phthalate, dipropyl phthalate, dibutyl phthalate, diisobutyl phthalate,
Examples include diamyl phthalate, diisoamyl phthalate, ethyl butyl phthalate, ethyl isobutyl phthalate and ethyl propyl phthalate.

The substance (b) is used in an amount of 0.01 g or more, preferably 0.01 to 0.2 ml, per 1 g of the substance (a).

The aliphatic hydrocarbon (c) (hereinafter simply referred to as (c) substance) and the aliphatic alcohol (e) (hereinafter simply referred to as (e) substance) are both liquid at -30 ° C to 50 ° C. It is.

(C) Preferred examples of the substance include aliphatic hydrocarbons having 5 to 12 carbon atoms such as pentane, hexane, heptane,
Octane, nonane, decane, dodecane and isomers thereof, and the like. Preferred examples of the substance (e) are aliphatic alcohols having 2 to 10 carbon atoms, for example, ethanol, propanol, butanol, pentanol, hexanol, octanol. And their isomers.

As the tetraalkoxytitanium of the above (d) (hereinafter simply referred to as the (d) substance), an alkoxy group having 1 to 10 carbon atoms is used, and particularly an alkoxy group having 3 or 4 carbon atoms is used. It is preferably used.

One or more kinds of the tetraalkoxy titanium can be used. (D) The amount of substance used is usually (a)
The total amount is in the range of 0.1 to 10 g per 1 g of the substance.

The phthalic dichloride (f) is used in an amount of 0.05 g or more, preferably 0.1 to 0.5 g, per 1 g of the substance (a).

The titanium tetrachloride (g) used in the present invention is used in an amount of 1 g or more, preferably 5 g or more, based on 1 g of the substance (a).

The contact temperature at this time is usually from 0 ° C to 130 ° C. The contact time is at least 10 minutes, preferably at least 30 minutes.

The obtained solid catalyst component (I) may be optionally washed with an organic solvent such as n-heptane and toluene,
Further, the treatment may be repeated with titanium tetrachloride (g).

All of these aspects are included in one aspect of the practice of the present invention.

A series of operations for preparing the solid catalyst component (I) in the present invention is preferably performed in the absence of oxygen, moisture and the like.

The solid catalyst component (I) prepared as described above is combined with the silicon compound (II) and the organoaluminum compound (III) to constitute the olefin-based polymerization catalyst according to the present invention. However, examples of the silicon compound (II) include alkoxysilane, phenylalkoxysilane, alkylalkoxysilane, cycloalkylalkoxysilane, and cycloalkylalkylalkoxysilane. Specific examples include tetramethoxysilane, tetraethoxysilane, Phenyltrimethoxysilane, phenyltriethoxysilane, phenyltripropoxysilane, phenyltriisopropoxysilane, diphenyldimethoxysilane, diphenyldiethoxysilane, ethyltrimethoxysilane, methyltrimethoxysilane, methyltriethoxy Examples include silane, ethyltriethoxysilane, ethyltriisopropoxysilane, vinyltriethoxysilane, vinyltrimethoxysilane, divinyldiethoxysilane, divinyldimethoxysilane, and the like.

Examples of the organoaluminum compound (III) include trialkylaluminum, dialkylaluminum halide, alkylaluminum dihalide, alkylaluminum sesquihalide, and mixtures thereof. Among them, trialkylaluminum is preferable. Triethylaluminum and triisobutylaluminum are particularly preferred.

The organoaluminum compound (III) is used in an amount of 1 to 1000 mol per g atom of titanium in the solid catalyst component, and the silicon compound is used in a molar ratio to the organoaluminum compound of 1 or less, preferably 0.005 to 1.0. Can be

The polymerization reaction using the polymerization catalyst according to the present invention can be carried out in the presence or absence of an organic solvent, and the olefin monomer used can be used in any state of gas and liquid. it can. Polymerization temperature is 20
0 ° C. or less, preferably 100 ° C. or less, the polymerization pressure is 100 kg /
cm ² · G or less, preferably 50 kg / cm ² · G or less.

The olefins homopolymerized or copolymerized using the olefin polymerization catalyst according to the present invention are ethylene, propylene, 1-butene and the like.

[Action and effect of the invention]

The olefin polymerization catalyst according to the present invention, when used for polymerization of olefins, exhibits an unexpectedly high activity, so that the amount of catalyst residues present in the produced polymer is extremely low. Since the amount of residual chlorine is extremely small, the effect of chlorine can be reduced to the extent that no deashing step is required for the product.

Chlorine remaining in the produced polymer causes corrosion of equipment used in processes such as granulation and molding, as well as deterioration of the produced polymer itself and yellowing. The gain is of great benefit to the art.

Further, according to the catalyst of the present invention, a large problem that an ester odor adheres to a produced polymer can be solved by not adding an organic carboxylic acid ester during polymerization.

Further, conventionally, there has been a common drawback in the so-called high activity supported catalyst, in which the activity per unit time of the catalyst is greatly reduced with the progress of polymerization, but in the catalyst according to the present invention, Since the decrease in activity with time is extremely small as compared with a conventionally known catalyst, it is also useful for extending the polymerization time such as copolymerization, and when a higher polymerization pressure is employed. Because of the large increase in the activity of the polymer, it can be widely used for bulk polymerization and gas-phase polymerization, which have recently attracted attention.

In addition, according to the catalyst of the present invention, a polymer having a high degree of stereoregularity with a regular shape can be obtained.

In addition, in industrial production of olefin polymers, it is generally accepted that hydrogen coexists during polymerization in terms of MI control and the like, but conventional magnesium chloride is used as a carrier and organic carboxylic acid esters are used. These catalysts had the disadvantage that the activity and stereoregularity were greatly reduced in the presence of hydrogen. However, when the polymerization of olefin is carried out in the presence of hydrogen using the catalyst according to the present invention,
Even when the MI of the resulting polymer is extremely high, the activity and stereoregularity do not decrease. Such an effect has been strongly desired by those skilled in the art.

In addition, it does not produce undesired finely divided polymer in the polyolefin production process, is suitable for gas phase polymerization, which has recently attracted attention, and has excellent fluidity, so-called post-polymerization process such as pumping and centrifugation. To facilitate
Since the particle shape is excellent, various effects can be exerted such that the granulation step can be omitted.

〔Example〕

Hereinafter, the present invention will be described more specifically with reference to examples.

Example 1 (1) (a) Preparation of substance A 2.0-liter round-bottom flask equipped with a stirrer was used, and the flask was sufficiently replaced with nitrogen gas. Then, 30 g of metallic magnesium powder, 1.0 g of iodine and n-butyl chloride were used. 1.2 l was charged and reacted at the boiling point of n-butyl chloride for 5 hours. After the reaction was completed, the supernatant was removed and the product was treated with 500 ml of n
After washing with -butyl chloride three times, the product was dried under reduced pressure to obtain a powdery substance.

(2) Preparation of solid catalyst component In a nitrogen gas atmosphere of 30 g of the powdery substance obtained in the above (1) and 1.5 ml of n-dibutyl phthalate, a stainless steel ball having a diameter of 25 mm was filled 4/5 of the total volume to a volume of 1.0 l. Of 1730 at a vibration frequency of 1430v.pm and a vibration of 3.5mm
Crushed for hours.

In a 500 ml round bottom flask equipped with a stirrer, take 10 g of the above crushed product and 70 ml of n-decane under a nitrogen gas atmosphere, heat to 80 ° C., charge 12 ml of tetrabutoxytitanium, and heat to 125 ° C. Then, the mixture was treated for 1 hour with stirring. Next, a solution obtained by mixing 25 ml of n-heptane and 7.1 ml of 2-ethylhexyl alcohol was added dropwise over a period of 30 minutes, and the mixture was reacted for 1 hour while maintaining the temperature at 125 ° C. Thereafter, the mixture was cooled to 80 ° C., and a mixed solution of 25 ml of n-heptane and 1.7 ml of phthalic chloride was added dropwise over a period of 30 minutes, followed by heating to 90 ° C. for 1 hour. The product obtained is washed 5 times with 200 ml of heptane and then TiCl ₄ 75
The mixture was added and reacted at 115 ° C. for 3 hours. 200ml after reaction
Was washed ten times with heptane to obtain a solid catalyst component.

At this time, when a titanium-containing machine in the solid catalyst component was measured, it was 3.88% by weight.

(3) Polymerization of Propylene Using an autoclave with an internal volume of 2.0 l equipped with a stirrer and completely replacing the gas with nitrogen gas, 200 mg of triethylaluminum, 45 mg of diphenyldimethoxysilane and 5.0 mg of the solid catalyst component were charged. Then, hydrogen gas 1.4
and 1.4 l of liquefied propylene, and a polymerization reaction was carried out at 70 ° C. for 1 hour. After the completion of the polymerization reaction, the produced polymer is heated to 80 ° C.
And dried under reduced pressure to obtain (A). Further, this was extracted with boiling n-heptane for 6 hours to obtain a polymer insoluble in n-heptane, and the amount of this was designated as (B).

The polymerization activity (C) per the solid catalyst component used is represented by the following formula.

The yield (D) of the whole crystalline polymer is represented by the following formula.

Further, the amount of residual chlorine in the produced polymer is represented by (E) and the MI of the produced polymer is represented by (F). The obtained results are shown in Table 1.

Example 2 An experiment was conducted in the same manner as in Example 1 except that the polymerization time was changed to 30 minutes. The results obtained are as shown in Table 1.

Example 3 An experiment was conducted in the same manner as in Example 1 except that the same amount of dipropyl phthalate was used instead of dibutyl phthalate. In this case, the titanium content in the solid catalyst component was 3.
It was 97% by weight. An experiment was conducted in the same manner as in Example 1 for the polymerization. The results obtained are shown in Table 1.

[Brief description of the drawings]

FIG. 1 is a schematic drawing for assisting understanding of the present invention.

Claims (1)

(57) [Claims] 1. A method comprising reacting (I) a metal magnesium powder with at least twice the molar amount of an alkyl monohalogen compound in the presence of iodine to obtain a substance (a) and a phthalic acid diester (b), which are obtained after pulverization. The resulting product was treated by sequentially adding tetraalkoxytitanium (d), aliphatic alcohol (e) and phthalic acid dichloride (f) at 70 ° C. or higher in the presence of an aliphatic hydrocarbon (c). A solid catalyst component obtained by adding titanium tetrachloride (g) to the resulting product and further treating the same; (II) a general formula SiRm (OR ′) 4-m (wherein R is an alkyl group, a cycloalkyl group, A vinyl group or an aryl group, and R 'is an alkyl group, when R is an alkyl group, the alkyl group may be the same as R';
Is 0 ≦ m <4. And (III) a general formula RnAlX3-n (wherein R is an alkyl group having 1 to 4 carbon atoms, X is any one of hydrogen, chlorine, bromine and iodine, and n is 0 <n ≦ 3. An olefin polymerization catalyst comprising an organoaluminum compound represented by the formula: