IP Library Granted Patent US 11,548,958
Granted Patent B2
US 11,548,958 · App. 17/748,116 · Granted Jan 10, 2023

Preparation of large pore silicas and uses thereof in chromium catalysts for olefin polymerization

Inventors: Max P. McDaniel (Bartlesville, OK); Kathy S. Clear (Bartlesville, OK); Carlton E. Ash (Owasso, OK); Stephen L. Kelly (Kingwood, TX); Amanda B. Allemand (The Woodlands, TX)
Assignee: Chevron Phillips Chemical Company LP
C08F10/02C08F2410/04
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Quick Facts
Patent No.
US 11,548,958
App. No.
17/748,116
Granted
Jan 10, 2023
Kind
B2
Abstract

Silica composites and supported chromium catalysts having a bulk density of 0.08 to 0.4 g/mL, a total pore volume of 0.4 to 2.5 mL/g, a BET surface area of 175 to 375 m 2 /g, and a peak pore diameter of 10 to 80 nm are disclosed herein. These silica composites and supported chromium catalysts can be formed by combining two silica components. The first silica component can be irregularly shaped, such as fumed silica, and the second silica component can be a colloidal silica or a silicon-containing compound, and the second silica component can act as a glue to bind the silica composite together.

Claims (47)

1. A process for preparing a silica composite, the process comprising:

(1) combining silica component I and silica component II in a diluent comprising at least about 70 wt. % water to form a mixture; and

(2) forming the silica composite in the mixture; wherein:

silica component I comprises irregular and non-spherical silica particles characterized by an average aspect ratio of at least about 2:1 and a BET surface area in a range from about 150 to about 1000 m 2 /g;

silica component II comprises a colloidal silica; and

the silica composite is characterized by:

a bulk density from about 0.08 to about 0.4 g/mL;

a total pore volume from about 0.4 to about 2.5 mL/g;

a BET surface area from about 175 to about 375 m 2 /g; and

a peak pore diameter from about 10 to about 80 nm.

2. The process of claim 1 , wherein silica component I comprises a fumed silica.

3. The process of claim 1 , further comprising:

combining a chromium-containing compound and an optional titanium-containing compound with the silica composite to form a supported chromium catalyst; and

calcining the supported chromium catalyst.

4. The process of claim 1 , wherein:

step (1) comprises combining a chromium-containing compound and an optional titanium-containing compound with silica component I and silica component II in the diluent to form the mixture; and

step (2) comprises forming a supported chromium catalyst in the mixture.

5. A process for preparing a silica composite, the process comprising:

(1) combining silica component I and silica component II in a solvent to form a mixture; and

(2) forming the silica composite in the mixture; wherein:

silica component I comprises a fumed silica;

silica component II comprises a silicon compound; and

the silica composite is characterized by:

a bulk density in a range from about 0.08 to about 0.4 g/mL;

a total pore volume from about 0.4 to about 2.5 mL/g;

a BET surface area from about 175 to about 375 m 2 /g; and

a peak pore diameter from about 10 to about 80 nm.

6. The process of claim 5 , wherein the silicon compound comprises a silicon alkoxide, a silicon halide, a silicon hydride, a silane, a hydrocarbyl silane, a siloxane, or any combination thereof.

7. The process of claim 5 , wherein the silicon compound comprises sodium silicate, an ethyl silicate, a silicate oligomer, or any combination thereof.

8. The process of claim 5 , further comprising:

combining a chromium-containing compound and an optional titanium-containing compound with the silica composite to form a supported chromium catalyst; and

calcining the supported chromium catalyst.

9. The process of claim 5 , wherein:

step (1) comprises combining a chromium-containing compound and an optional titanium-containing compound with silica component I and silica component II in the solvent to form the mixture; and

step (2) comprises forming a supported chromium catalyst in the mixture.

10. The process of claim 1 , wherein the colloidal silica has a d50 particle size from about 3 to about 25 nm.

11. The process of claim 1 , wherein an amount of silica component II, based on total amount of silica component I and silica component II, is from about 2 to about 25 wt. %.

12. The process of claim 1 , wherein silica component I is non-porous.

13. The process of claim 1 , wherein the average aspect ratio is from about 3:1 to about 50:1.

14. The process of claim 1 , wherein step (1) comprises combining a titanium-containing compound with silica component I and silica component II in the diluent.

15. The process of claim 3 , wherein the supported chromium catalyst comprises from about 0.5 to about 5 wt. % chromium, based on the total weight of the catalyst.

16. The process of claim 4 , wherein the supported chromium catalyst comprises from about 0.5 to about 5 wt. % chromium, based on the total weight of the catalyst.

17. The process of claim 5 , wherein an amount of silica component II, based on total amount of silica component I and silica component II, is from about 10 to about 90 wt. %.

18. The process of claim 5 , wherein silica component I is non-porous.

19. The process of claim 5 , wherein step (1) comprises combining a titanium-containing compound with silica component I and silica component II in the solvent.

20. The process of claim 8 , wherein the supported chromium catalyst comprises from about 0.5 to about 5 wt. % chromium, based on the total weight of the catalyst.

21. The process of claim 9 , wherein the supported chromium catalyst comprises from about 0.5 to about 5 wt. % chromium, based on the total weight of the catalyst.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 2, 2022
From: MCDANIEL, MAX P.; CLEAR, KATHY S.; ASH, CARLTON E.; KELLY, STEPHEN L.; ALLEMAND, AMANDA B.
To: CHEVRON PHILLIPS CHEMICAL COMPANY LP
Reel/Frame 060079/0738 →
Continuity (3)
Division 17476556 · Sep 16, 2021
Division 16421529 · May 24, 2019
Related Publication 20220275116A1 · Sep 1, 2022
Cited By (2)
US 12,528,890 US 12,570,770