IP Library Granted Patent US 9,611,145
Granted Patent B2
US 9,611,145 · App. 14/120,973 · Granted Apr 4, 2017

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: Greyrock Energy, Inc.
C01B3/40B01J23/755C07C1/22C07C29/153C10G2/332C10G2/333C10J1/20C10L1/08C22C19/07B01J23/78C01B2203/0233C01B2203/0238C01B2203/0244C01B2203/0261C01B2203/0283C01B2203/061C01B2203/062C01B2203/1058C01B2203/1241Y02P20/52Y02P30/30
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Quick Facts
Patent No.
US 9,611,145
App. No.
14/120,973
Granted
Apr 4, 2017
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 (11)

1. A solid solution catalyst for the production of syngas from carbon dioxide and light hydrocarbons, wherein the catalyst comprises a single transition metal in the form of Ni 2 O and wherein the catalyst contains 5-20 wt. % Ni.

2. The catalyst of claim 1 in which the catalyst has a high thermal stability up to 1,100° C.

3. The catalyst of claim 1 which has good resistance to contaminants that may be present in captured CO 2 streams, natural gas, biogas or other gas feedstock streams.

4. The catalyst of claim 1 that does not require the use of precious metals.

5. The catalyst of claim 1 in which the catalyst does not form (coking) during the CO 2 reforming processes.

6. The catalyst of claim 1 which efficiently produces syngas under dry reforming conditions using selected mixtures of CO 2 and CH 4 .

7. The catalyst of claim 1 which efficiently produces syngas under dry reforming conditions using selected mixtures of CO 2 and C 2 + hydrocarbons.

8. The catalyst of claim 1 which efficiently produces syngas under dry/steam reforming conditions using selected mixtures of CH 4 , CO 2 and H 2 O.

9. The catalyst of claim 1 which efficiently produces syngas under dry/steam reforming conditions using selected mixtures of C 2 + hydrocarbons, CO 2 and H 2 O.

10. The catalyst of claim 1 which efficiently produces syngas under tri-reforming conditions using selected mixtures of CH 4 , CO 2 , H 2 O and O 2 .

11. The catalyst of claim 1 which efficiently produces syngas under tri-reforming conditions using selected mixtures of C 2 + hydrocarbons, CO 2 , H 2 O and O 2 .

Assignments (4)
CHANGE OF NAME Recorded Sep 24, 2020
From: CARBON RECYCLING SOLUTIONS, LLC
To: INFINIUM TECHNOLOGY, LLC
Reel/Frame 053879/0573 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 13, 2019
From: GREYROCK TECHNOLOGY, LLC
To: CARBON RECYCLING SOLUTIONS, LLC
Reel/Frame 048591/0547 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 28, 2017
From: GREYROCK ENERGY, INC.
To: GREYROCK TECHNOLOGY, LLC
Reel/Frame 044183/0429 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 8, 2014
From: SCHUETZLE, ROBERT; SCHUETZLE, DENNIS
To: GREYROCK ENERGY, INC.
Reel/Frame 034563/0186 →
Continuity (2)
Provisional Application 61958235 · Jul 22, 2013
Related Publication 20150031922A1 · Jan 29, 2015