IP Library Granted Patent US 7,700,513
Granted Patent B2
US 7,700,513 · App. 11/753,471 · Granted Apr 20, 2010

Supported catalyst for olefin polymerization

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Quick Facts
Patent No.
US 7,700,513
App. No.
11/753,471
Granted
Apr 20, 2010
Kind
B2
Abstract

Disclosed are catalyst systems and methods of making the catalyst systems for the polymerization of an olefin containing a solid titanium catalyst component containing an inorganic titanium compound, a magnesium alcohol adduct made from an inorganic magnesium compound and an alcohol, and a porous support having at least one of a certain specific surface area, a certain pore volume, and a certain median particle size. The catalyst system may further contain an organoaluminum compound and optionally an organosilicon compound. Also disclosed are methods of making polyolefins.

Claims (30)

1. A solid titanium catalyst component for the polymerization of olefins, comprising:

an inorganic titanium compound;

a magnesium alcohol adduct made by contacting an inorganic magnesium compound, an alcohol, and an organic medium, wherein the alcohol and the inorganic magnesium compound are contacted at a molar ratio of the alcohol to the inorganic magnesium compound from about 0.1:1 to about 1:0.1, and wherein the organic medium and the inorganic magnesium compound are contacted at a molar ratio of the organic medium to the inorganic magnesium compound from about 1:1 to about 50:1; and

a porous support having at least one of a specific surface area of about 100 m 2 /g or more and about 2,000 m 2 /g or less, a pore volume of about 0.2 cc/g or more and about 5 cc/g or less, and a median particle size (by volume) of about 1 micron or more and about 200 microns or less,

the solid titanium catalyst component having a diameter from about 20 microns to about 150 microns (on a 50% by volume basis).

2. The solid titanium catalyst component of claim 1 , wherein the porous support has at least two of a specific surface area of about 200 m 2 /g or more and about 1,500 m 2 /g or less, a pore volume of about 0.3 cc/g or more and about 4 cc/g or less, and a median particle size (by volume) of about 5 microns or more and about 150 microns or less.

3. The solid titanium catalyst component of claim 1 , wherein the porous support has a specific surface area of about 300 m 2 /g or more and about 1,000 m 2 /g or less, a pore volume of about 0.5 cc/g or more and about 3 cc/g or less, and a median particle size (by volume) of about 10 microns or more and about 100 microns or less.

4. The solid titanium catalyst component of claim 1 , wherein the porous support comprises at least one selected from the group consisting of silica, alumina, alumina-silicates, ceria, zeolites, clay, zirconia, titania, zinc oxide.

5. The solid titanium catalyst component of claim 1 , wherein the inorganic magnesium compound is at least one selected from the group consisting of magnesium chloride, magnesium bromide, magnesium iodide, and magnesium fluoride, and the inorganic titanium compound comprises at least one selected from the group consisting of titanium chloride, titanium bromide, titanium iodide, and titanium fluoride.

6. The solid titanium catalyst component of claim 1 , wherein the alcohol comprises an alkyl alcohol containing from 1 to about 12 carbon atoms.

7. The solid titanium catalyst component of claim 1 further comprising an internal electron donor.

8. The solid titanium catalyst component of claim 1 , wherein the magnesium alcohol adduct is not dealcoholed.

9. The solid titanium catalyst component of claim 1 , wherein the porous support comprises at least one selected from the group consisting of silica, alumina, alumina-silicates, ceria, zeolites, clay, zirconia, titania, zinc oxide.

10. The solid titanium catalyst component of claim 1 , wherein the alcohol comprises an alkyl alcohol containing from 1 to about 12 carbon atoms.

11. The solid titanium catalyst component of claim 1 , wherein the magnesium-alcohol adduct is made by contacting the alcohol and the inorganic magnesium at a molar ratio of the alcohol to the inorganic magnesium compound of about 0.1:1 to about 1:0.1.

12. A solid titanium catalyst component for the polymerization of olefins, consisting essentially of:

an inorganic titanium compound; a magnesium alcohol adduct made from an inorganic magnesium compound and an alcohol; and

a porous support having at least one of a specific surface area of about 100 m 2 /g or more and about 2,000 m 2 /g or less, a pore volume of about 0.2 cc/g or more and about 5 cc/g or less, and a median particle size (by volume) of about 1 micron or more and about 200 microns or less,

the solid titanium catalyst component having a diameter from about 20 microns to about 150 microns (on a 50% by volume basis).

13. A method of making a solid titanium catalyst component for the polymerization of olefins, comprising:

combining an inorganic magnesium compound, an alcohol, and an organic medium to form a magnesium alcohol adduct, wherein the alcohol and the inorganic magnesium compound are contacted at a molar ratio of the alcohol to the inorganic magnesium compound from about 0.1:1 to about 1:0.1, and wherein the organic medium and the inorganic magnesium compound are contacted at a molar ratio of the organic medium to the inorganic magnesium compound from about 1:1 to about 50:1;

impregnating the adduct onto a porous support having at least one of a specific surface area of about 100 m 2 /g or more and about 2,000 m 2 /g or less, a pore volume of about 0.2 cc/g or more and about 5 cc/g or less, and a median particle size (by volume) of about 1 micron or more and about 200 microns or less; and

contacting the adduct impregnated porous support with an inorganic titanium compound.

14. The method of claim 13 , wherein the porous support has a specific surface area of about 300 m 2 /g or more and about 1,000 m 2 /g or less, a pore volume of about 0.5 cc/g or more and about 3 cc/g or less, and a median particle size (by volume) of about 10 microns or more and about 100 microns or less.

15. The method of claim 13 , wherein the porous support comprises at least one selected from the group consisting of silica, alumina, alumina-silicates, ceria, zeolites, clay, zirconia, titania, and zinc oxide.

16. The method of claim 13 , wherein the inorganic magnesium compound is at least one selected from the group consisting of magnesium chloride, magnesium bromide, magnesium iodide, and magnesium fluoride, and the inorganic titanium compound comprises at least one selected from the group consisting of titanium chloride, titanium bromide, titanium iodide, and titanium fluoride.

17. The method of claim 13 , wherein the magnesium compound and the alcohol are heated to a temperature from about 40° C. to about 200° C.

18. The method of claim 13 , wherein the inorganic magnesium compound and the alcohol are heated for a time from about 5 minutes to about 15 hours.

19. The method of claim 13 , wherein the magnesium alcohol adduct is made by contacting the alcohol and the inorganic magnesium compound at a molar ratio of the alcohol to the inorganic magnesium compound from about 0.25:1 to about 1:0.25.

20. The method of claim 13 , wherein the organic medium is one or more selected from the group consisting of butane, pentane, hexane, heptane, octanes, decane, kerosene, cyclopentane, cyclohexane, cyclooxtane, benzene, tolune, xylene, ethylbenzene, and napthalenes.

Assignments (11)
NOTES SECURITY INTEREST Recorded Jan 29, 2026
From: W. R. GRACE & CO.-CONN.; ADVANCED REFINING TECHNOLOGIES LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS NOTES COLLATERAL AGENT
Reel/Frame 074532/0229 →
SECURITY INTEREST Recorded Aug 19, 2025
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 072519/0240 →
SECURITY AGREEMENT (NOTES) Recorded Aug 19, 2025
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS NOTES COLLATERAL AGENT
Reel/Frame 072520/0653 →
SECURITY INTEREST Recorded Aug 19, 2025
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 072519/0265 →
SECURITY INTEREST Recorded Apr 2, 2023
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 063199/0472 →
NOTES SECURITY AGREEMENT Recorded Sep 23, 2021
From: W. R. GRACE & CO.-CONN.
To: WILMINGTON TRUST, NATIONAL ASSOCIATION
Reel/Frame 057594/0156 →
RELEASE OF SECURITY INTEREST Recorded Sep 23, 2021
From: GOLDMAN SACHS BANK USA
To: W. R. GRACE & CO.-CONN.
Reel/Frame 057594/0026 →
TERM LOAN SECURITY AGREEMENT Recorded Sep 23, 2021
From: W. R. GRACE & CO.-CONN.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 057594/0104 →
SECURITY INTEREST Recorded Apr 3, 2018
From: W. R. GRACE & CO.-CONN.
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 045828/0683 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 22, 2016
From: BASF CORPORATION
To: W. R. GRACE & CO. - CONN.
Reel/Frame 040255/0136 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 25, 2007
From: ZHU, ZHIDONG; CHANG, MAIN
To: BASF CATALYSTS LLC
Reel/Frame 019344/0277 →