Electrochemically mediated gas capture, including from low concentration streams
US-2021062351-A1 · Mar 4, 2021 · US
US12005392B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12005392-B2 |
| Application number | US-202217685285-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 2, 2022 |
| Priority date | Oct 27, 2015 |
| Publication date | Jun 11, 2024 |
| Grant date | Jun 11, 2024 |
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The present disclosure generally relates to apparatuses, systems, and methods for separating a target species (e.g., CO 2 ) from a gas mixture (e.g., gas stream) via an electrochemical process.
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What is claimed is: 1. A method of treating a gas stream, the method comprising: applying a first potential difference across at least one negative electrode and a positive electrode of an electrochemical cell, wherein the at least one negative electrode comprises a first electroactive species, the positive electrode comprises a second electroactive species, and the electrochemical cell comprises a separator positioned between the at least one negative electrode and the positive electrode, wherein the separator comprises: (a) a conductive electrolyte having a room temperature vapor pressure of less than 10 −5 Pa; and/or (b) a room temperature ionic liquid; and introducing a gas stream comprising a target species comprising an aprotic acidic gas to the electrochemical cell to bond the target species to the first electroactive species to produce a treated gas stream; and applying a second, different potential difference across the at least one negative electrode and the positive electrode of the electrochemical cell to release the target species from the first electroactive species to produce a target species-rich gas stream; wherein: the application of the first potential difference causes a reduction reaction resulting in at least some of the first electroactive species being in a reduced state; the target species bonds to the first electroactive species in the reduced state to produce the treated gas stream; the application of the second potential difference causes an oxidation reaction at the at least one negative electrode resulting in the oxidation of at least some of the first electroactive species in the reduced state bonded to the target species; the target species is released from the oxidized first electroactive species to produce the target species-rich gas stream; and the first electroactive species comprises a quinone. 2. The method of claim 1 , wherein the separator comprises a conductive electrolyte having a room temperature vapor pressure of less than 10 −5 Pa. 3. The method of claim 2 , wherein the conductive electrolyte comprises a conductive liquid having a room temperature vapor pressure of less than 10 −5 Pa. 4. The method of claim 1 , wherein the separator comprises a room temperature ionic liquid. 5. The method of claim 1 , wherein the first electroactive species is immobilized on and/or within the at least one negative electrode. 6. The method of claim 1 , wherein the first electroactive species comprises a polymeric quinone. 7. The method of claim 1 , wherein the aprotic acidic gas comprises carbon dioxide, sulfur dioxide, a borane, or a combination thereof. 8. The method of claim 7 , wherein the aprotic acidic gas comprises carbon dioxide. 9. The method of claim 8 , wherein the first electroactive species comprises polyanthraquinone. 10. The method of claim 1 , wherein the at least one negative electrode is porous. 11. The method of claim 1 , wherein the target species bonds to the first electroactive species in the reduced state via a covalent bond. 12. The method of claim 3 , wherein the first electroactive species is immobilized on and/or within the at least one negative electrode. 13. The method of claim 12 , wherein the first electroactive species comprises a polymeric quinone. 14. The method of claim 13 , wherein the aprotic acidic gas comprises carbon dioxide, sulfur dioxide, a borane, or a combination thereof. 15. The method of claim 14 , wherein the aprotic acidic gas comprises carbon dioxide. 16. The method of claim 15 , wherein the at least one negative electrode is porous. 17. The method of claim 16 , wherein the concentration of carbon dioxide in the gas stream introduced to the electrochemical cell is between 10 ppm and 500 ppm. 18. The method of claim 4 , wherein the first electroactive species is immobilized on and/or within the at least one negative electrode. 19. The method of claim 18 , wherein the first electroactive species comprises a polymeric quinone. 20. The method of claim 19 , wherein the aprotic acidic gas comprises carbon dioxide, sulfur dioxide, a borane, or a combination thereof. 21. The method of claim 20 , wherein the aprotic acidic gas comprises carbon dioxide. 22. The method of claim 21 , wherein the at least one negative electrode is porous. 23. The method of claim 22 , wherein the concentration of carbon dioxide in the gas stream introduced to the electrochemical cell is between 10 ppm and 500 ppm. 24. The method of claim 3 , wherein the first electroactive species comprises a polymeric quinone. 25. The method of claim 24 , wherein the aprotic acidic gas comprises carbon dioxide, sulfur dioxide, a borane, or a combination thereof. 26. The method of claim 25 , wherein the aprotic acidic gas comprises carbon dioxide. 27. The method of claim 26 , wherein the at least one negative electrode is porous. 28. The method of claim 27 , wherein the concentration of carbon dioxide in the gas stream introduced to the electrochemical cell is between 10 ppm and 500 ppm. 29. The method of claim 4 , wherein the first electroactive species comprises a polymeric quinone. 30. The method of claim 29 , wherein the aprotic acidic gas comprises carbon dioxide, sulfur dioxide, a borane, or a combination thereof. 31. The method of claim 30 , wherein the aprotic acidic gas comprises carbon dioxide. 32. The method of claim 31 , wherein the at least one negative electrode is porous. 33. The method of claim 32 , wherein the concentration of carbon dioxide in the gas stream introduced to the electrochemical cell is between 10 ppm and 500 ppm. 34. The method of claim 3 , wherein the at least one negative electrode is porous. 35. The method of claim 4 , wherein the at least one negative electrode is porous. 36. The method of claim 1 , wherein the concentration of the target species in the gas stream introduced to the electrochemical cell is between 10 ppm and 500 ppm.
characterised by the material · CPC title
with diaphragms · CPC title
Organic compound · CPC title
Carbon dioxide · CPC title
of CO2 · CPC title
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