# US 5,348,925 A · Catalyst for the polymerization of olefins

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- Number: US 5,348,925 A
- Document ID: US5348925A
- Status: Granted
- Kind: A
- Application number: 08/020,990
- Filed: 1993-02-22
- Granted: 1994-09-20
- Earliest claimed: 1992-02-26
- Assignees: ECP Enichem Polimeri S.r.l.
- Inventors: Federico Milani; Luciano Luciani; Antonio Labianco
- Web page: https://patentgrep.com/patent/US5348925A

## CPC

- C08F 10/00: Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS

## Abstract

A solid component of catalyst, active in the polymerization of propylene and other .alpha.-olefins in stereoregular polymers, is obtained: (i) by treating a non-activated silica support in particles with a tin tetrahalide, to at least partially block the hydroxylic groups of the silica and to obtain a blocked silica; (ii) by impregnating the blocked silica with magnesium dialkyl or magnesium alkyl halide to make the magnesium compound react with the tin compound and with possible residual hydroxylic groups of the silica and to obtain a support; (iii) by halogenating the support by contact with a halogenating agent selected from the halides of tin, antimonium or silicon to obtain a halogenated support; (iv) by titanating the halogenated support with an excess of a titanium tetrahalide to obtain a titanated support; (v) by putting the titanated support in contact with a Lewis base, to obtain a solid component of catalyst.

## Claims

### Claim 1

Process for the preparation of a solid component of catalyst, active in the polymerization of propylene and other .alpha.-olefins in stereoregular polymers, said solid component containing silica, magnesium, halogen, titanium and a Lewis base, said process comprising:
(i) treating a non-activated particulate silica support, by contacting said silica with a solution, in an inert hydrocarbon solvent, of a tin tetrahalide, operating with a weight ratio between the tin tetrahalide and the silica of between 1:1 and 20:1, at a temperature ranging from -30.degree. C. to 30.degree. C., for a time which is sufficient to at least partially block the hydroxylic groups of the silica, to obtain a blocked silica;
impregnating said blocked silica with a solution, in an inert hydrocarbon solvent, of a magnesium dialkyl or magnesium alkyl halide, operating with a weight ratio between the magnesium compound and the blocked silica of between 0.1:1 and 10:1, at a temperature ranging from 20.degree. C. to the boiling point of the liquid phase, for a time which is sufficient to interact the magnesium compound with the tin compound and with any possible residual hydroxylic groups of the silica, to obtain a support;
(iii) halogenating said support by contacting said support with a solution, in an inert hydrocarbon solvent, of a halogenating agent selected from the halides of tin, antimony or silicon, operating with a molar ratio between the halogenating agent and the magnesium compound introduced in step (ii) ranging from 0.1:1 to 100:1, at a temperature ranging from -20.degree. to 100.degree. C. and for a period of 0.5 to 5.0 hours, to obtain a halogenated support;
(iv) titanating said halogenated support by contacting said halogenated support with an excess of a titanium tetrahalide, in the form of either a liquid or as a solution in an inert hydrocarbon solvent, operating at a temperature ranging from 20.degree. to 120.degree. C. and for a period of 0.5 to 5.0 hours, to obtain a titanated support;
(v) contacting said titanated support with a Lewis base, in the from of either a liquid or as a solution in an inert hydrocarbon solvent, operating with a molar ratio between said Lewis base and the magnesium compound introduced in step (ii) ranging from 0.05:1 to 0.5:1, at a temperature ranging from 80.degree. to 120.degree. C. and for a period of 0.5 to 5.0 hours, to obtain a solid component of catalyst; and
(vi) recovering said solid component of catalyst from the reaction products of step (v).

### Claim 2 (depends on 1)

Process according to claim 1, characterized in that said silica used in step (i) is a microspheroidal, porous silica, with a particle size ranging from 20 to 100 .mu.m, with a surface area of 150 to 400 m.sup.2 /g, with a pore volume of 1.3 to 1.8 ml/g and with an average pore diameter of 20 to 30 A (angstrom), containing hydroxyls and water in a total quantity which is higher than 1% by weight up to a maximum value of about 5% by weight.

### Claim 3 (depends on 1)

Process according to claim 1, characterized in that in step (i) tin tetrachloride is used, operating with a solvent selected from pentane, isopentane, hexane, heptane and octane, at a temperature increasing from about -20.degree. C. to room temperature (20.degree.-25.degree. C.), for a period of 1 to 3 hours.

### Claim 4 (depends on 1)

Process according to claim 1, characterized in that in step (ii) a magnesium compound is used having either one of the formulae MgRR' or MgR"X, wherein R, R' and R" each independently represent an alkyl group, linear or branched, containing from 1 to 12 carbon atoms and X represents a halogen atom.

### Claim 5 (depends on 4)

Process according to claim 4 characterized in that in step (ii) is carried out in a hydrocarbon solvent selected from the group consisting of pentane, isopentane, hexane, heptane and octane, with a weight ratio between the magnesium compound and silica ranging from 0.2:1 to 2.0:1, and preferably within the range of 1.0:1-1.5:1, at a temperature equal or close to room temperature (20.degree.-25.degree. C.) and for a period of 0.5 hours.

### Claim 6 (depends on 1)

Process according to claim 1, characterized in that in step (iii) the halogenating agent is selected from tin tetrachloride, antimonium pentachloride and silicon tetrachloride, operating in a solvent selected from pentane, isopentane, hexane, heptane and octane, with a molar ratio between the halogenating agent and magnesium compound ranging from 1:1 to 20:1 and for a period of 1-2 hours.

### Claim 7 (depends on 1)

Process according to claim 1, characterized in that the reaction temperature ranges from -30.degree. to 70.degree. C. when the halogenating agent is a tin or antimonium halide, and from 40.degree. to 100.degree. C. when the halogenating agent is a silicon halide.

### Claim 8 (depends on 1)

Process according to claim 1, characterized in that step (iv) is carried out with titanium tetrachloride, at a temperature ranging from 80.degree. to 100.degree. C. and for a period of 1-2 hours, to obtain a titanated support containing from 3 to 7% by weight of titanium.

### Claim 9 (depends on 1)

Process according to claim 1, characterized in that in step (v) the Lewis base is selected from aromatic esters, alkyl esters of benzoic acid, p-methoxybenzoic acid and p-toluic acid, aliphatic esters, alkyl aryl silanes and alkoxysilanes, operating in a solvent selected from pentane, isopentane, hexane, heptane and octane, with a molar ratio between the Lewis base and magnesium compound ranging from 0.1:1 to 0.3:1, at a temperature of about 90.degree. C., for a period of about 1 hour.

### Claim 10 (depends on 9)

Process according to claim 9, characterized in that said Lewis base is selected from diisobutylphthalate, diethyl carbonate, ethyl pivalate, ethyl acetate and dimethyl maleate.

### Claim 11 (depends on 1)

A solid component of catalyst produced according to the process of claim 1.

### Claim 12 (depends on 11)

Catalyst for the stereospecific polymerization of propylene and other .alpha.-olefins formed of: (A) a solid component of catalyst according to claim 11, wherein said solid component contains silica, 4-8% by weight of magnesium, 10-35% by weight of chlorine, 3-7% by weight of titanium and 1-15% by weight of a Lewis base, wherein 5-10% of the titanium is in a trivalent state and the remaining part is in a tetravalent state (B) an aluminum trialkyl or aluminium alkyl halide and (C) an electron donor compound capable of forming a complex compound with component (B).

### Claim 13 (depends on 12)

Catalyst according to claim 12, characterized in that component (B) is selected from aluminium triethyl, aluminium tributyl, aluminium triisobutyl and aluminium trihexyl and component (C) is selected from alkoxy silanes defined with the formula R.sup.1 R.sup.2 Si(OR.sup.3)(OR.sup.4) wherein R.sup.1 and R.sup.2 are phenyl groups and R.sup.3 and R.sup.4 are C.sub.1 -C.sub.4 alkyl groups, the atomic ratio between the aluminium, present in component (B) and the titanium, present in component (A), varying from 10/1 to 1000/1 and the molar ratio between components (B) and (C) varying from 5/1 to 20/1.

### Claim 14 (depends on 4)

A process according to claim 4, wherein the halogen is chlorine.

### Claim 15 (depends on 4)

A process according to claim 4, wherein the magnesium compound is selected from magnesium diethyl, magnesium ethylbutyl, magnesium dihexyl, magnesium butyloctyl and magnesium dioctyl.

### Claim 16 (depends on 5)

A process according to claim 5, wherein the weight ratio between the magnesium compound and silica is within the range of 1.0:1-1.5:1.

### Claim 17 (depends on 13)

A catalyst according to claim 13, wherein the siloxane is dimethoxy diphenyl silane.

### Claim 18 (depends on 13)

A catalyst according to claim 13, wherein the atomic ratio between the aluminum and the titanium is from 50/1 to 150/1.

### Claim 19 (depends on 13)

A catalyst according to claim 13, wherein the molar ratio between components (B) and (C) is about 10/1.

### Claim 20 (depends on 11)

A solid component of catalyst according to claim 11, comprising silica, 4-8% by weight of magnesium, 10-35% by weight of chlorine, 3-7% by weight of titanium and 1-15% by weight of a Lewis base, wherein 5-10% of the titanium is in a trivalent state and the remaining part of the titanium is in a tetravalent state.