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US4186107A Expired / Lapsed US ⏱️ 0.0 years remaining

Solid catalyst component for olefin polymerization

Assignee: Himont Inc
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Filing: 1978-04-14
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Granted: 1980-01-29
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Expires: 1998-04-14
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Abstract

Abstract The transition metal component of a Ziegler-Natta catalyst is composed of a titanium halide deposited on a magnesium halide support. The support is prepared by a process involving reaction of a dialkyl magnesium with an alkyl aluminum halide in a hydrocarbon solvent and including treatment of the magnesium halide formed in the reaction with an electron donor, preferably a dialkyl ether.

Inventors

  • 👤 Kalus P. Wagner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 16:16
CPC Classifications
C; C08; C08F; C08F4/00; C08F4/02; C08F4/022; C08F10/00

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 455 words
A process for the preparation of a solid catalyst component for use in the polymerization of 1-olefins, which component is composed of a titanium halide deposited on an essentially anhydrous magnesium halide support, said process comprising the steps, carried out in an inert atmosphere, of (1) dissolving a compound having the formula R 2 Mg, where R is a C 2 -C 20 alkyl group, in a hydrocarbon solvent or a mixture of the hydrocarbon solvent with an electron donor, (2) dissolving a compound having the formula R' n AlX 3-n , wherein R' is a C 1 -C 20 alkyl group, X is a chlorine or bromine atom and n is 1 or 2, in a hydrocarbon solvent or a mixture of the hydrocarbon solvent with an electron donor, (3) contacting the resulting solutions from steps (1) and (2) with each other at a temperature of from about -65° C. to about 30° C. for a period of from about 0.5 to about 5 hours, thereby forming a suspension in the solvent of magnesium halide particles ranging from about 0.05 to about 80 microns in size, (4) isolating said particles from said suspension, (5) successively washing said particles with a hydrocarbon solvent until the particles are substantially free of halide and residual aluminum compounds, (6) contacting said particles with an electron donor before and/or after said particles are successively washed with hydrocarbon solvent, with the proviso that step (6) may be omitted when an electron donor is present in step (1) and/or step (2), (7) washing the donor-treated particles with a hydrocarbon solvent, (8) contacting the washed particles with an alkyl ester of an aromatic acid, wherein the ester contains a total of 8 to 24 carbon atoms, and with a titanium halide, thereby effecting deposition of said titanium halide on the magnesium halide particles, (9) contacting the resulting particles with an electron donor and (10) washing the donor-treated particles with a hydrocarbon solvent, said hydrocarbon solvent being selected from the group consisting of C 5 -C 12 aliphatic hydrocarbons, C 5 -C 12 monocyclic cycloaliphatic hydrocarbons, C 6 -C 12 monocyclic aromatic hydrocarbons and mixtures thereof, and said electron donor being selected from the group consisting of C 4 -C 24 aliphatic ethers, C 3 -C 4 cyclic ethers, C 7 -C 15 aromatic ethers, C 4 -C 24 alkyl esters of fatty acids, C 8 -C 24 alkyl esters of aromatic acids, C 1 -C 12 aliphatic amines, C 4 -C 6 cyclic amines, C 6 -C 10 aromatic amines, C 1 -C 18 aliphatic alcohols, C 7 -C 15 aromatic alcohols, C 6 -C 10 phenols, C 6 -C 18 aliphatic or aromatic phosphines and C 6 -C 12 aliphatic sulfides.
Claim 2
Dependent Claim 455 words
A process for the preparation of a solid catalyst component for use in the polymerization of 1-olefins, which component is composed of a titanium halide deposited on an essentially anhydrous magnesium halide support, said process comprising the steps, carried out in an inert atmosphere, of (1) dissolving a compound having the formula R 2 Mg, where R is a C 2 -C 20 alkyl group, in a hydrocarbon solvent or a mixture of the hydrocarbon solvent with an electron donor, (2) dissolving a compound having the formula R' n AlX 3-n , wherein R' is a C 1 -C 20 alkyl group, X is a chlorine or bromine atom and n is 1 or 2, in a hydrocarbon solvent or a mixture of the hydrocarbon solvent with an electron donor, (3) contacting the resulting solutions from steps (1) and (2) with each other at a temperature of from about -65° C. to about 30° C. for a period of from about 0.5 to about 5 hours, thereby forming a suspension in the solvent of magnesium halide particles ranging from about 0.05 to about 80 microns in size, (4) isolating said particles from said suspension, (5) successively washing said particles with a hydrocarbon solvent until the particles are substantially free of halide and residual aluminum compounds, (6) contacting said particles with an electron donor before and/or after said particles are successively washed with hydrocarbon solvent, with the proviso that step (6) may be omitted when an electron donor is present in step (1) and/or step (2), (7) washing the donor-treated particles with a hydrocarbon solvent, (8) contacting the washed particles with an alkyl ester of an aromatic acid, wherein the ester contains a total of 8 to 24 carbon atoms, and with a titanium halide, thereby effecting deposition of said titanium halide on the magnesium halide particles, (9) contacting the resulting particles with an electron donor and (10) washing the donor-treated particles with a hydrocarbon solvent, said hydrocarbon solvent being selected from the group consisting of C 5 -C 12 aliphatic hydrocarbons, C 5 -C 12 monocyclic cycloaliphatic hydrocarbons, C 6 -C 12 monocyclic aromatic hydrocarbons and mixtures thereof, and said electron donor being selected from the group consisting of C 4 -C 24 aliphatic ethers, C 3 -C 4 cyclic ethers, C 7 -C 15 aromatic ethers, C 4 -C 24 alkyl esters of fatty acids, C 8 -C 24 alkyl esters of aromatic acids, C 1 -C 12 aliphatic amines, C 4 -C 6 cyclic amines, C 6 -C 10 aromatic amines, C 1 -C 18 aliphatic alcohols, C 7 -C 15 aromatic alcohols, C 6 -C 10 phenols, C 6 -C 18 aliphatic or aromatic phosphines and C 6 -C 12 aliphatic sulfides.
Claim 3
Dependent Claim 20 words
The process of claim 1 wherein the Al/Mg mole ratio in step (3) is from about 1:1 to about 10:1.
Claim 4
Dependent Claim 16 words
The process of claim 1 wherein the hydrocarbon is a C 5 -C 12 aliphatic hydrocarbon.
Claim 5
Dependent Claim 23 words
The process of claim 1 wherein R 2 Mg is n-butyl sec-butyl magnesium, n-butyl ethyl magnesium or di-n-butyl magnesium complexed with triethyl aluminum.
Claim 6
Dependent Claim 14 words
The process of claim 1 wherein R' n AlX 3-n is ethyl aluminum dichloride.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein the electron donor is a C 4 -C 24 aliphatic ether.
Claim 8
Dependent Claim 14 words
The process of claim 6 wherein the ether is di-n-butyl ether or diisoamyl ether.
Claim 9
Dependent Claim 15 words
The process of claim 6 wherein the ether is present in steps (1) or (2).
Claim 10
Dependent Claim 13 words
The process of claim 6 wherein the ether is present in step (6).
Claim 11
Dependent Claim 15 words
The process of claim 1 wherein the ester used in step (8) is ethyl benzoate.

References Cited (Backward Citations)

US3642746A Cited
GB1373981A Cited
US3953414A Cited
BE849503A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-01-28 1983-07-30 1984-01-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-01-28 1987-07-30 1988-01-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-01-28 1991-07-30 1992-01-29 $7700.00 Window Closed / Lapsed

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