IP Library Granted Patent US 9,840,446
Granted Patent B2
US 9,840,446 · App. 15/303,928 · Granted Dec 12, 2017

Process for production of methane-containing gas mixture

Inventor: Peter Edward James Abbott (Cleveland, GB)
Assignee: Johnson Matthey Public Limited Company
C07C1/0435C07C1/04C07C1/12C07C7/14816C10G2/332C10K3/02C10L3/08C10L3/101C07C2523/46C07C2523/755C10L2290/141
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Quick Facts
Patent No.
US 9,840,446
App. No.
15/303,928
Granted
Dec 12, 2017
Kind
B2
Abstract

A process for producing a methane-containing gas mixture includes the steps of: (i) passing a first feed gas mixture including hydrogen and carbon dioxide through a bed of methanation catalyst to react a portion of the hydrogen with at least a portion of the carbon dioxide and form a methane-containing gas mixture containing residual hydrogen, (ii) adding an oxygen-containing gas to the methane-containing gas mixture containing residual hydrogen to form a second feed gas mixture, and (iii) passing the second feed gas mixture through a bed of an oxidation catalyst to react the residual hydrogen and oxygen to form a hydrogen depleted methane-containing gas mixture.

Claims (16)

1. A process for producing a methane-containing gas mixture comprising the steps of:

(i) passing a first feed gas mixture comprising hydrogen and carbon dioxide through a bed of methanation catalyst to react a portion of the hydrogen with at least a portion of the carbon dioxide and form a methane-containing gas mixture containing residual hydrogen,

(ii) adding an oxygen-containing gas to the methane-containing gas mixture containing residual hydrogen to form a second feed gas mixture, and

(iii) passing the second feed gas mixture through a bed of a selective oxidation catalyst at an inlet temperature in the range 150 to 350° C. to selectively react the residual hydrogen and oxygen to form a hydrogen depleted methane-containing gas mixture.

2. The process according to claim 1 , wherein the hydrogen concentration in the first feed gas mixture is 20% by volume.

3. The process according to claim 1 , wherein the first feed gas mixture is a synthesis gas comprising hydrogen, carbon dioxide and carbon monoxide.

4. The process according to claim 1 , wherein the first feed gas mixture is a prepared by mixing a hydrogen-containing gas mixture with a carbon dioxide-containing gas mixture.

5. The process according to claim 4 , wherein the hydrogen-containing gas mixture is a methane-containing gas mixture.

6. The process according to claim 4 , wherein the first feed gas mixture or hydrogen-containing gas mixture and/or the carbon dioxide-containing gas mixture are subjected to a desulphurisation step prior to the methanation step.

7. The process according to claim 1 , wherein the methanation catalyst is a ruthenium- or nickel-containing methanation catalyst.

8. The process according to claim 1 , wherein the methanation catalyst is operated at an inlet temperature in the range 200 to 350° C.

9. The process according to claim 1 , wherein the temperature of the methane-containing gas mixture containing residual hydrogen is adjusted before mixing it with the oxygen containing gas.

10. The process according to claim 1 , wherein the oxidation catalyst is a supported precious metal oxidation catalyst.

11. The process according to claim 1 , wherein the process is performed at a pressure in the range 5 to 80 bar abs.

12. The process according to claim 1 , wherein the methanation catalyst is operated at an inlet temperature in the range 200 to 300° C.

13. The process according to claim 1 , wherein the methanation catalyst is operated at an inlet temperature in the range 230 to 280° C.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 26, 2025
From: JOHNSON MATTHEY PLC
To: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
Reel/Frame 072941/0488 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 9, 2017
From: ABBOTT, PETER EDWARD JAMES
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 040901/0058 →
Priority Claims (1)
GB 1406890.2 · Apr 16, 2014 · national
Continuity (1)
Related Publication 20170022121A1 · Jan 26, 2017