Seawater plant with inclined aeration and mixed auto recovery
US-2016368795-A1 · Dec 22, 2016 · US
US10625204B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10625204-B2 |
| Application number | US-201716311174-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 19, 2017 |
| Priority date | Jun 19, 2016 |
| Publication date | Apr 21, 2020 |
| Grant date | Apr 21, 2020 |
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This invention is directed to a method used to remove gases from industrial exhaust streams, and in particular, to a method for removing sulfur dioxide from flue gases, with molten carbonate and treating the resulting molten mixture with a natural gas and optionally with an oxidant.
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What is claimed is: 1. A method for removing sulfur dioxide from flue gas, said method comprises: providing a flue gas comprising a sulfur dioxide; absorbing said sulfur dioxide with molten carbonate forming a molten mixture of carbonates sulfites and sulfates at a temperature of between 400° C. to 600° C.; treating said molten mixture with a natural gas and optionally with an oxidant, by passing said natural gas through said molten mixture, thereby producing a sulfur containing vapor, cooling said sulfur containing vapor and collecting it. 2. The method of claim 1 , wherein said step of forming molten mixture of carbonates comprises: melting eutectic mixture of Li, Na, K or combination thereof with said flue gas. 3. The method of claim 1 , wherein said oxidant is O 2 , air, oxygen enriched air. 4. The method of claim 1 , wherein said sulfur containing vapor is H 2 S, SO 2 , SO 3 . 5. The method of claim 3 , wherein said sulfur containing vapor is further converted to solid or liquid sulfur containing material for further use. 6. The method of claim 1 , wherein said treating said molten mixture with a natural gas comprises; heating said molten to a temperature of between 400° C. to 1000° C. 7. The method of claim 1 , wherein said natural gas comprises methane, ethane, propane, butane, pentane, acetylene, nitrogen or combination thereof. 8. The method of claim 1 , wherein said molten mixture of carbonates, sulfites and sulfates is treated with natural gas and optionally with an oxidant simultaneously. 9. The method of claim 1 , wherein said molten mixture of carbonates, sulfites and sulfates is treated with said natural gas first followed by the treatment of said oxidant. 10. The method of claim 1 , wherein 0.01-0.5 m 3 of natural gas per 1 kg of sulfates or sulfites are passed through the molten mixture. 11. The method of claim 1 , wherein said absorbing step is conducted by stirring under flow of bubbling gas. 12. The method of claim 1 , wherein said absorbing step and treating step are conducted in two different zones; wherein said first zone comprises a scrubbing chamber for the absorbing step and said second zone comprises a regeneration chamber for the treating step and said zones are connected via hydraulic communication. 13. The method of claim 12 wherein the scrubbing chamber being configured for scrubbing the flue gas by absorbing the sulfur dioxide in a pool to form a molten mixture of carbonates, sulfites and sulfates in the pool. 14. The method of claim 12 , wherein the regeneration chamber being configured for producing a sulfur-containing vapor; and comprising a sulfur-containing vapor outlet port configured for controllable release of the sulfur-containing vapor obtained therein. 15. The method of claim 13 , wherein said scrubbing chamber comprises a plurality of baffles arranged within said scrubbing chamber and configured to provide a flow of said flue gas within the scrubbing zone. 16. The method of claim 1 , wherein said absorbing step and treating step are conducted in one zone; wherein said one zone acts as a scrubbing chamber for the absorbing step and as a regeneration chamber for the treating step. 17. The method of claim 16 wherein the scrubbing chamber being configured for scrubbing the flue gas by absorbing the sulfur dioxide in a pool to form a molten mixture of carbonates, sulfites and sulfates in the pool. 18. The method of claim 16 , wherein the regeneration chamber being configured for producing a sulfur-containing vapor; and comprising a sulfur-containing vapor outlet port configured for controllable release of the sulfur-containing vapor obtained therein. 19. The method of claim 16 , wherein said scrubbing chamber comprises a plurality of baffles arranged within said scrubbing chamber and configured to provide a flow of said flue gas within the scrubbing zone.
by treating the gases with other liquids · CPC title
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