IP Library Granted Patent US 8,124,798
Granted Patent B2
US 8,124,798 · App. 12/653,678 · Granted Feb 28, 2012

Direct epoxidation catalyst and process

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Quick Facts
Patent No.
US 8,124,798
App. No.
12/653,678
Granted
Feb 28, 2012
Kind
B2
Abstract

A catalyst, useful for the direct epoxidation of olefins, is disclosed. The catalyst comprises palladium nanoparticles, support nanoparticles, and a titanium zeolite having a particle size of 2 microns or greater. The palladium nanoparticles are deposited on the support nanoparticles to form supported palladium nanoparticles, and the supported palladium nanoparticles are deposited on the titanium zeolite; or the supported palladium nanoparticles are deposited on a carrier having a particle size of 2 microns or greater. The invention also includes a process for producing an epoxide comprising reacting an olefin, hydrogen and oxygen in the presence of the catalyst. The catalysts are more active in epoxidation reactions, while demonstrating the same or better selectivity.

Claims (23)

1. A process for producing an epoxide comprising reacting an olefin, hydrogen and oxygen in the presence of a catalyst comprising palladium nanoparticles, support nanoparticles having an average crystallite size of less than 200 nm, and a titanium zeolite having a particle size of 2 microns or greater, wherein the palladium nanoparticles are deposited on the support nanoparticles to form supported palladium nanoparticles, and:

(a) the supported palladium nanoparticles are deposited on the titanium zeolite; or

(b) the supported palladium nanoparticles are deposited on a carrier having a particle size of 2 microns or greater.

2. The process of claim 1 wherein the titanium zeolite is a titanium silicalite.

3. The process of claim 1 wherein the support nanoparticles are selected from the group consisting of titania, zirconia, niobia, silica, alumina, tantalum oxide, and mixtures thereof.

4. The process of claim 1 wherein the carrier is selected from the group consisting of titania, zirconia, niobia, silica, alumina, silica-alumina, tantalum oxide, titania-silica, zirconia-silica, niobia-silica, and mixtures thereof.

5. The process of claim 4 wherein the carrier is titania.

6. The process of claim 4 wherein the carrier has a particle size of 5 microns or greater.

7. The process of claim 1 wherein the olefin is a C 2 -C 6 olefin.

8. The process of claim 1 wherein the catalyst further comprises lead.

9. A catalyst comprising palladium nanoparticles, support nanoparticles having an average crystallite size of less than 200 nm, and a titanium zeolite having a particle size of 2 microns or greater, wherein the palladium nanoparticles are deposited on the support nanoparticles to form supported palladium nanoparticles, and:

(a) the supported palladium nanoparticles are deposited on the titanium zeolite; or

(b) the supported palladium nanoparticles are deposited on a carrier having a particle size of 2 microns or greater.

10. The catalyst of claim 9 wherein the support nanoparticles are selected from the group consisting of titania, zirconia, niobia, silica, alumina, tantalum oxide, and mixtures thereof.

11. The catalyst of claim 9 wherein the titanium zeolite is TS-1 or Ti-MWW.

12. The catalyst of claim 9 wherein the carrier is selected from the group consisting of titania, zirconia, niobia, silica, alumina, silica-alumina, tantalum oxide, titania-silica, zirconia-silica, niobia-silica, and mixtures thereof.

13. The catalyst of claim 9 wherein the carrier is titania.

14. The catalyst of claim 9 wherein the carrier has a particle size of 5 microns or greater.

15. The catalyst of claim 9 wherein the catalyst further comprises lead, gold, or platinum.

16. The process of claim 1 wherein the average crystallite size of the support nanoparticles is from 0.5 to 100 nm.

17. The process of claim 1 wherein the average crystallite size of the support nanoparticles is from 3 to 60 nm.

18. The catalyst of claim 9 wherein the average crystallite size of the support nanoparticles is from 0.5 to 100 nm.

19. The catalyst of claim 9 wherein the average crystallite size of the support nanoparticles is from 3 to 60 nm.

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 4, 2010
From: GREY, ROGER A.; COCHRAN, ROBERT N.; LE-KHAC, BI
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 023903/0292 →