IP Library Granted Patent US 10,478,806
Granted Patent B2
US 10,478,806 · App. 15/530,981 · Granted Nov 19, 2019

Process and catalyst system for the production of high quality syngas from light hydrocarbons and carbon dioxide

Inventors: Robert Schuetzle (Sacramento, CA); Dennis Schuetzle (Grass Valley, CA)
Assignee: Carbon Recycling Solutions, LLC
B01J23/755C01B3/40C01B3/48C07C1/22C07C29/153C10G2/332C10G2/333C10J1/20C10L1/08C22C19/07B01J23/78C01B2203/0233C01B2203/0238C01B2203/0244C01B2203/0261C01B2203/0283C01B2203/061C01B2203/062C01B2203/1058C01B2203/1241Y02P20/52Y02P30/30
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Quick Facts
Patent No.
US 10,478,806
App. No.
15/530,981
Granted
Nov 19, 2019
Kind
B2
Abstract

The present invention describes a process and catalysts for the conversion of a light hydrocarbon and carbon dioxide input stream into high quality syngas with the subsequent conversion of the syngas into fuels or chemicals. In one aspect, the present invention provides an efficient, solid solution catalyst for the production of a carbon containing gas from carbon dioxide and light hydrocarbons. The catalyst comprises a single transition metal, and the transition metal is nickel.

Claims (10)

1. A nickel-based, solid solution catalyst for producing syngas, wherein the solid solution catalyst is not coated on a substrate, and wherein the catalyst is in contact with CO 2 , CH 4 and H 2 O, and wherein the catalyst is capable of producing syngas with a pre-selected ratio of H 2 /CO, and wherein the H 2 /CO ratio is capable of being varied based on the production process used to produce the syngas, wherein the nickel-based, solid solution catalyst comprises only one transition metal, and wherein the transition metal is nickel.

2. The nickel-based, solid solution catalyst according to claim 1 , wherein the nickel-based, solid solution catalyst is stable up to 1,100° C.

3. The nickel-based, solid solution catalyst according to claim 1 , wherein the nickel-based, solid solution catalyst does not include a precious metal.

4. The nickel-based, solid solution catalyst according to claim 1 , wherein the catalyst formulation is capable of producing syngas with a H 2 /CO ratio ranging from 1.5 to 2.5.

5. The nickel-based, solid solution catalyst according to claim 1 , wherein the catalyst formulation is capable of producing syngas with a H 2 /CO ratio ranging from 0.7 to 1.0.

6. A nickel-based, solid solution catalyst for producing syngas, wherein the solid solution catalyst is not coated on a substrate, and wherein the catalyst is in contact with CO 2 , CH 4 , H 2 O and O 2 , and wherein the catalyst is capable of producing syngas with a pre-selected ratio of H 2 /CO, and wherein the H 2 /CO ratio is capable of being varied based on the production process used to produce the syngas, wherein the nickel-based, solid solution catalyst comprises only one transition metal, and wherein the transition metal is nickel.

7. The nickel-based, solid solution catalyst according to claim 6 , wherein the nickel-based, solid solution catalyst is stable up to 1,100° C.

8. The nickel-based, solid solution catalyst according to claim 6 , wherein the nickel-based, solid solution catalyst does not include a precious metal.

9. The nickel-based, solid solution catalyst according to claim 6 , wherein the catalyst formulation is capable of producing syngas with a H 2 /CO ratio ranging from 1.5 to 2.5.

10. The nickel-based, solid solution catalyst according to claim 6 , wherein the catalyst formulation is capable of producing syngas with a H 2 /CO ratio ranging from 0.7 to 1.0.

Assignments (2)
CHANGE OF NAME Recorded Sep 24, 2020
From: CARBON RECYCLING SOLUTIONS, LLC
To: INFINIUM TECHNOLOGY, LLC
Reel/Frame 053880/0379 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 13, 2019
From: GREYROCK TECHNOLOGY, LLC
To: CARBON RECYCLING SOLUTIONS, LLC
Reel/Frame 048591/0547 →
Continuity (3)
Continuation 14120973 · Jul 16, 2014
Provisional Application 61958235 · Jul 22, 2013
Related Publication 20170246618A1 · Aug 31, 2017
Cited By (1)
US 12,258,272