IP Library Granted Patent US 8,124,555
Granted Patent B2
US 8,124,555 · App. 12/658,029 · Granted Feb 28, 2012

Process for making titanium-MWW zeolite

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Quick Facts
Patent No.
US 8,124,555
App. No.
12/658,029
Granted
Feb 28, 2012
Kind
B2
Abstract

Titanium-MWW zeolite is prepared by heating a gel formed from a titanium compound, a silicon source, a boron source, an MWW-templating agent, and water at a temperature in the range of 35° C. to 75° C. for a period of 8 to 30 hours to form a pre-crystallized gel, and heating the pre-crystallized gel to a temperature in the range of 160° C. to 190° C. for a period of 5 or more days to form the titanium-MWW zeolite. The zeolite, after it is contacted with an acid, is useful in olefin epoxidation with hydrogen peroxide.

Claims (26)

1. A process for producing a crystalline titanium-MWW zeolite, which comprises:

a) heating a gel formed from a titanium compound, a silicon source, a boron source, an MWW-templating agent, and water at a temperature in the range of 35° C. to 75° C. for a period of 8 to 30 hours to form a pre-crystallized gel; and

b) heating the pre-crystallized gel at a temperature in the range of 160° C. to 190° C. for a period of 5 to 8 days to form the crystalline titanium-MWW zeolite.

2. The process of claim 1 wherein the titanium compound is selected from the group consisting of titanium halides, titanium alkoxides, and mixtures thereof.

3. The process of claim 2 wherein the titanium alkoxide is selected from the group consisting of titanium tetraethoxide, titanium tetraisopropoxide, titanium tetrabutoxide, and mixtures thereof.

4. The process of claim 1 , wherein the silicon source is selected from the group consisting of colloidal silica, fumed silica, silicon alkoxides, and mixtures thereof.

5. The process of claim 4 wherein the silicon alkoxide is selected from the group consisting of tetraethylorthosilicate, tetramethylorthosilicate, and mixtures thereof.

6. The process of claim 1 wherein the boron source is selected from the group consisting of boric acid, boron halides, boron hydrides, borate esters, metal borates, and mixtures thereof.

7. The process of claim 1 wherein the MWW-templating agent is piperidine or hexamethyleneimine.

8. The process of claim 1 wherein the pre-crystallized gel is heated at a temperature in the range of 120° C. to 155° C. for a period of 8 to 30 hours prior to heating at a temperature in the range of 160° C. to 190° C.

9. A process comprising reacting an olefin and hydrogen peroxide in the presence of a crystalline titanium-MWW zeolite, wherein the crystalline titanium-MWW zeolite is produced by:

a) heating a gel formed from a titanium compound, a silicon source, a boron source, an MWW-templating agent, and water at a temperature in the range of 35° C. to 75° C. for a period of 8 to 30 hours to form a pre-crystallized gel;

b) heating the pre-crystallized gel to a temperature in the range of 160° C. to 190° C. for a period of 5 to 8 days to form the titanium-MWW zeolite; and

c) contacting the titanium-MWW zeolite with an acid.

10. The process of claim 9 wherein the titanium compound is selected from the group consisting of titanium halides, titanium alkoxides, and mixtures thereof; the silicon source is selected from the group consisting of colloidal silica, fumed silica, silicon alkoxides, and mixtures thereof; the boron source is selected from the group consisting of boric acid, boron halides, boron hydrides, borate esters, metal borates, and mixtures thereof and the MWW-templating agent is piperidine or hexamethyleneimine.

11. The process of claim 9 wherein the acid is selected from the group consisting of nitric acid and sulfuric acid.

12. The process of claim 9 wherein the pre-crystallized gel is heated at a temperature in the range of 120° C. to 155° C. for a period of 8 to 30 hours prior to heating at a temperature in the range of 160° C. to 190° C.

13. The process of claim 9 wherein reaction of olefin and hydrogen peroxide is performed in a solvent selected form the group consisting of methanol, ethanol, isopropanol, tert-butanol, water, and mixtures thereof.

14. The process of claim 9 wherein the hydrogen peroxide is formed by the in situ reaction of hydrogen and oxygen in the presence of a noble metal catalyst.

15. The process of claim 1 wherein the crystalline titanium-MWW zeolite produced has an activity greater than 20 grams POE produced per gram of catalyst per hour.

16. A process for producing a crystalline titanium-MWW zeolite, which comprises:

a) heating a gel formed from a titanium compound, a silicon source, a boron source, an MWW-templating agent, and water at a temperature in the range of 50° C. to 70° C. for a period of 12 to 18 hours to form a pre-crystallized gel; and

b) heating the pre-crystallized gel at a temperature of 170° C. for a period of 5 to 7 days to form the crystalline titanium-MWW zeolite.

17. The process of claim 16 wherein the pre-crystallized gel is heated at a temperature of 150° C. for a period of 12 to 24 hours prior to heating at a temperature of 170° C.

18. The process of claim 16 wherein the pre-crystallized gel is heated at a temperature of 130° C. for a period of 8 to 12 hours followed by heating at a temperature of 150° C. for a period of 12 to 24 hours prior to heating at a temperature of 170° C.

19. The process of claim 16 wherein the crystalline titanium-MWW zeolite produced has an activity greater than 20 grams POE produced per gram of catalyst per hour.

Assignments (10)
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032123/0799 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: CITIBANK, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032125/0296 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032137/0156 →
APPOINTMENT OF SUCCESSOR ADMINISTRATIVE AGENT Recorded Jan 23, 2014
From: UBS AG, STAMFORD BRANCH
To: BANK OF AMERICA, N.A.
Reel/Frame 032137/0639 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: BANK OF AMERICA, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032138/0134 →
SECURITY AGREEMENT Recorded May 19, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 024402/0681 →
SECURITY AGREEMENT Recorded May 18, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 024397/0818 →
SECURITY AGREEMENT Recorded May 7, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 024342/0801 →
SECURITY AGREEMENT Recorded May 6, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: DEUTSCHE BANK TRUST COMPANY AMERICAS, AS COLLATERAL AGENT
Reel/Frame 024342/0421 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 1, 2010
From: MANDIMUTSIRA, BEAVEN S.; MILLER, JAY F.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 023958/0876 →