IP Library Granted Patent US 10,308,565
Granted Patent B2
US 10,308,565 · App. 15/647,806 · Granted Jun 4, 2019

Catalysts for petrochemical catalysis

Inventors: Wayne P. Schammel (Brisbane, CA); Anja Rumplecker (San Francisco, CA); Joel M. Cizeron (Redwood City, CA); Erik C. Scher (San Francisco, CA); Fabio R. Zurcher (Brisbane, CA); Greg Nyce (Pleasanton, CA); Jarod McCormick (San Carlos, CA); Marian Alcid (Sunnyvale, CA); Joel Gamoras (Vallejo, CA); Daniel Rosenberg (San Francisco, CA); Erik-Jan Ras (Amsterdam, NL)
Assignee: Silura Technologies, Inc.
C07C2/84B01J23/10B01J23/34B01J23/8892B01J35/06B01J37/03B01J37/084B01J37/088C07C2/78B01J2523/00C07C2521/06C07C2521/08C07C2521/10C07C2523/02C07C2523/10C07C2523/30C07C2523/34C07C2523/75C07C2523/889Y02P20/52
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Quick Facts
Patent No.
US 10,308,565
App. No.
15/647,806
Granted
Jun 4, 2019
Kind
B2
Abstract

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Claims (17)

1. A method for the oxidative coupling of methane, the method comprising contacting methane with a catalyst at temperatures ranging from about 550° C. to about 750° C., thereby converting the methane to C2 hydrocarbons at a methane conversion of greater than 20% and a C2 selectivity of greater than 50%, wherein the catalyst comprises the following formula:

ABO 3 ;

wherein:

A is an element from the lanthanides or groups 2, 3 or 4 of the periodic table;

B is an element from groups 4, 12 or 13 of the periodic table or Ce, Eu, Gd, Tb or Ho; and

O is oxygen,

the catalyst further comprising one or more dopant from any one of groups 2 or 3, and provided that A and B are not the same.

2. The method of claim 1 , wherein the method produces a product gas comprising less than 0.5% carbon monoxide.

3. The method of claim 1 , wherein A is from groups 2, 3 or 4.

4. The method of claim 1 , wherein A is Ce, Pr, Sr, Ca, Mg, Y, Zr or Ba.

5. The method of claim 1 , wherein B is from group 4.

6. The method of claim 1 , wherein B is Zr or Hf.

7. The method of claim 1 , wherein the dopant is Sr, Mg or Ca.

8. The method of claim 1 , wherein the catalyst comprises one of the following formulas: Y/SrZrO 3 , SrHfO 3 , SrZrO 3 , Mg/SrHfO 3 , CaHfO 3 or SrTbO 3 .

9. The method of claim 1 , wherein the catalyst is a bulk catalyst.

10. The method of claim 1 , wherein the catalyst is a nanostructured catalyst.

11. The method of claim 10 , wherein the catalyst is a nanowire.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 22, 2021
From: SILURIA TECHNOLOGIES, INC.
To: SILURIA, LLC
Reel/Frame 055358/0122 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 22, 2021
From: SILURIA, LLC
To: LUMMUS TECHNOLOGY LLC
Reel/Frame 055358/0158 →
Continuity (4)
Continuation 14995135 · Jan 13, 2016
Continuation 14212435 · Mar 14, 2014
Provisional Application 61794486 · Mar 15, 2013
Related Publication 20180093931A1 · Apr 5, 2018
Cited By (5)
US 12,227,466 US 12,447,465 US 12,589,381 US 12,612,344 US 12,655,075