Process for enabling carbon-capture from existing combustion processes
A process of producing a feed from a solid oxide electrolysis cell. A first portion of the flue gas produced from a combustion process is directed to the anode side of the solid oxide electrolysis cell. The feed and a second portion of the flue gas are then mixed to produce an enhanced feed. The enhanced feed is then mixed with fuel and combusted in the combustion process to produce flue gas. The flue gas comprises greater than 50 wt % CO 2 and less than 1 wt % N 2 .
1. A process comprising:
producing a feed from a solid oxide electrolysis cell;
directing a first portion of the flue gas produced from a combustion process, to the anode side of the solid oxide electrolysis cell;
mixing the feed and a second portion of the flue gas to produce an enhanced feed, wherein
the second portion of the flue gas is at least 1 wt % of the enhanced feed; and
combusting the enhanced feed in the combustion process to produce flue gas,
wherein the flue gas comprises greater than 50 wt % CO 2 and less than 1 wt % N 2 .
2. The process of claim 1 , wherein the combustion process is either a steam methane reformer furnace or a fluidized catalytic cracker regenerator.
3. The process of claim 2 , wherein the steam methane reforming furnace is an oxygen-fuel steam methane reforming furnace.
4. The process of claim 1 , wherein the feed and the flue gas is mixed with natural gas prior to combustion by the combustion process.
5. The process of claim 1 , wherein air is added to the combustion process.
6. The process of claim 5 , wherein up to 99 wt % air compared to the enhanced feed is added to the combustion process.
7. The process of claim 5 , wherein the enhanced feed is mixed with natural gas and air prior to combustion by the combustion process.
8. The process of claim 1 , wherein the flue gas does not contain any nitrogen.
9. The process of claim 1 , wherein the production of the feed occurs at ambient pressure.
10. The process of claim 1 , wherein the flue gas does not undergo any subsequent nitrogen separation step.
11. The process of claim 1 , wherein the feed produced from the solid oxide electrolysis cell contains greater than 95 wt % oxygen.
12. The process of claim 1 , wherein the feed produced from the solid oxide electrolysis cell is 100 wt % oxygen.
13. The process of claim 1 , wherein at least 25 wt % of the flue gas is directed to the anode side of the solid oxide electrolysis cell.
14. The process of claim 1 , wherein at least 50 wt % of the flue gas is directed to the anode side of the solid oxide electrolysis cell.
15. The process of claim 1 , wherein a portion of the flue gas is directed to the anode side of the solid oxide electrolysis cell and a portion is fed directly into the combustion process.
16. The process of claim 1 , wherein a portion of the flue gas is directed to the anode side of the solid oxide electrolysis cell and a portion undergoes direct CO 2 capture.
17. The process of claim 1 , wherein a portion of the flue gas is directed to the anode side of the solid oxide electrolysis cell, a portion is fed directly into the combustion process and a portion undergoes direct CO 2 capture.
18. A process comprising:
directing a first portion of the flue gas, at least 50 wt %, produced from a combustion process, to the anode side of a solid oxide electrolysis cell;
producing a feed from the solid oxide electrolysis cell; and
mixing the feed and a second portion of the flue gas to produce an enhanced feed, wherein
the second portion of the flue gas is at least 1 wt % of the enhanced feed;
mixing the enhanced feed with a fuel; and
combusting the enhanced feed and the fuel in the combustion process to produce flue gas wherein the flue gas comprises greater than 75 wt % CO 2 and less than 1 wt % N 2 .