IP Library › Granted Patent US 8,865,780
Granted Patent B2
US 8,865,780 · App. 13/808,118 · Granted Oct 21, 2014

Process for converting biogas to a gas rich in methane

Inventor: John Bogild Hansen (Copenhagen Ø, DK)
Assignee: Haldor Topsoe A/S
C07C1/0485C25B1/04Y02E60/366C25B3/04C01B2203/042C25B1/02Y02E50/343C01B3/56C01B2203/0485C10L3/08
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Quick Facts
Patent No.
US 8,865,780
App. No.
13/808,118
Granted
Oct 21, 2014
Kind
B2
Abstract

Process for converting biogas to a gas rich in methane comprising the steps of: —mixing a carbon dioxide-comprising biogas with steam to form a mixture comprising carbon dioxide, methane and steam; electrolysing the mixture comprising carbon dioxide, methane and steam in a high temperature solid oxide electrolyser cell unit, to obtain a gas comprising mainly hydrogen and carbon monoxide; catalytically converting hydrogen and carbon monoxide in the gas comprising hydrogen and carbon monoxide to methane in one or more methanation steps to obtain a gas rich in methane.

Claims (21)

1. Process for converting biogas to a gas rich in methane comprising the steps of:

mixing a carbon dioxide-comprising biogas with steam to form a mixture comprising carbon dioxide, methane and steam;

electrolysing the mixture comprising carbon dioxide, methane and steam in a high temperature solid oxide electrolyser cell unit, to obtain a gas comprising mainly hydrogen and carbon monoxide; and

catalytically converting hydrogen and carbon monoxide in the gas comprising hydrogen and carbon monoxide to methane in one or more methanation steps to obtain a gas rich in methane.

2. Process according to claim 1 , wherein the one or more methanation steps include adiabatic methanation followed by non-adiabatic methanation.

3. Process according to claim 1 , wherein the mixture comprising carbon dioxide, biogas and steam also comprises approximately 0.1-200 ppm of sulphide compound.

4. Process according to claim 1 , wherein the gas comprising hydrogen and carbon monoxide is desulphurised after electrolysis and prior to methanation.

5. Process according to claim 1 , wherein the mixture comprising biogas, carbon dioxide and steam is co-electrolysed according to the following reactions:

CO 2 =CO+0.5O 2   (1)

H 2 O=H 2 +0.5O 2   (2).

6. Process according to claim 1 , wherein the high temperature solid oxide electrolyser cell unit comprises fuel electrode material with limited or no steam reforming activity.

7. Process according to claim 6 , wherein the fuel electrode material does not comprise nickel or the fuel electrode material is all ceramic.

8. Process according to claim 6 , wherein the fuel electrode material comprises compounds or elements selected from the group consisting of LSCM, Cu, CeO 2 , titanates and combinations thereof.

9. Process according to claim 6 , wherein the fuel electrode material comprises Ni-YSZ, SYSZ or Ni-SSZ electrodes having a thickness of less than or equal to 10 microns.

10. Process according to claim 1 , wherein the high temperature solid oxide electrolyser cell unit operates thermoneutrally.

11. Process according to claim 2 , wherein the sulphide is removed from the hydrogen-rich gas by absorption on a metal oxide absorbent.

12. Process according to claim 11 , wherein the metal oxide absorbent is zinc oxide and/or is based on copper.

13. Process according to claim 1 , wherein carbon monoxide and hydrogen are converted to methane in a methanation step according to the following reactions:

CO+3H 2 =CH 4 +H 2 O  (3)

CO 2 +4H 2 =CH 4 +2H 2 O  (4).

14. Process according to claim 1 , wherein the one or more methanation steps are catalysed by a catalyst including metals selected from the group consisting of Group 6B, Group 8 of the Periodic Table and combinations thereof.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 3, 2013
From: BOGILD HANSEN, JOHN
To: HALDOR TOPSOE A/S
Reel/Frame 029559/0424 →
Continuity (1)
Related Publication 20130109767A1 · May 2, 2013