Impact of membrane characteristics on the performance and cycling of the br2-h2 redox flow cell
US-2017244127-A1 · Aug 24, 2017 · US
US11646434B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11646434-B2 |
| Application number | US-201916980549-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 12, 2019 |
| Priority date | Mar 12, 2018 |
| Publication date | May 9, 2023 |
| Grant date | May 9, 2023 |
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An organic flow battery having a positive electrode electrolyte containing organic compounds with extended conjugation and/or cyclic side chains is provided. The flow battery includes a positive electrode and a positive electrode electrolyte including first solvent and a first redox couple. The positive electrode electrolyte flows over and contacting the positive electrode. The first redox couple includes a first organic compound and a reduction product of the first organic compound. The flow battery also includes a negative electrode and a negative electrode electrolyte including a second solvent and a second redox couple. The negative electrode electrolyte flows g over and contacts the positive electrode. Typically, an ion exchange membrane is interposed between the positive electrode and the negative electrode Characteristically, the first organic compound resists crossover through the ion exchange membrane.
Opening claim text (preview).
What is claimed is: 1. A flow battery comprising: a positive electrode; a positive electrode electrolyte including water and a first redox couple, the positive electrode electrolyte flowing over and contacting the positive electrode, the first redox couple including a first organic compound Q 1 and a reduction product H 2 Q 1 of the first organic compound, a negative electrode; a negative electrode electrolyte including water and a second redox couple, the negative electrode electrolyte flowing over and contacting the positive electrode; and an ion exchange membrane interposed between the positive electrode and the negative electrode, wherein the first organic compound resists crossover through the ion exchange membrane and wherein the first organic compound has formulae 2, 3, 4, or 5: wherein m, n, o, p are each independently 0, 1, 2, 3, or 4; q and r are each independently 0, 1, or 2; s and t are each independently 0, 1, 3, or 4; R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are each independently —H, —R′, —NO 2 , —NH 2 , —N(R′R″) 2 , —N(R′R″R′″) 3 + L − , —CF 3 , —CCl 3 , —CN, —SO 3 H, —PO 3 H 2 , —COOH, —CO 2 R′, —COR′, —CHO, —OH, —OR′, —O − M + , —SO 3 − M + , —PO 3 − M + , —COO − M + , —CF 2 H, —CF 2 R′, —CFH 3 , and —CFR′R″ where R′, R″ and R′″ are alkyl or aryl groups; L is any negatively charged counter ion; and M is any positively charged counter ion. 2. The flow battery of claim 1 wherein the second redox couple includes a second organic compound, the first organic compound having a standard electrode potential that is at least 0.3 volts higher than a standard electrode potential for the second organic compound. 3. The flow battery of claim 2 wherein the first organic compound has a standard electrode potential that is at least 0.1 V positive to a mercury/mercurous sulfate electrode (MSE) for the positive electrode electrolyte. 4. The flow battery of claim 3 wherein the second organic compound has a standard electron potential at least 0.1 V negative to the MSE for the negative electrode electrolyte. 5. The flow battery of claim 1 wherein the first organic compound has an acidity greater than the acidity of the ion exchange membrane. 6. The flow battery of claim 1 wherein R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are each independently —H or C 1-6 alkyl. 7. The flow battery of claim 1 wherein R 1 , R 2 , R 3 , R 4 , R 5 , R 6 , R 7 , R 8 , R 9 , R 10 , R 11 and R 12 are each independently —H. 8. A flow battery comprising: a positive electrode; a positive electrode electrolyte including water and a first redox couple, the positive electrode electrolyte flowing over and contacting the positive electrode, the first redox couple including a first organic compound Q 1 and a reduction product H 2 Q 1 of the first organic compound; a negative electrode; a negative electrode electrolyte including water and a second redox couple, the negative electrode electrolyte flowing over and contacting the positive electrode; and an ion exchange membrane interposed between the positive electrode and the negative electrode, wherein the first organic compound has formulae 6 or 7: wherein i and k are each independently 0, 1, or 2; R 13 and R 14 are each independently —H, —R′, —NO 2 , —NH 2 , —N(R′R″) 2 , —N(R′R″R′″) 3 + L − , —CF 3 , —CCl 3 , —CN, —SO 3 H, —PO 3 H 2 , —COOH, —CO 2 R′, —COR′, —CHO, —OH, —OR′, —O − M + , —SO3 − M + , —PO 3 − M + , —COO − M + , —CF 2 H, —CF 2 R′, —CFH 3 , and —CFR′R″ where R′, R″ and R′″ are alkyl or aryl groups; Y is —(CH2) n , —(CH2OCH2) n , SO, SO 2 , other substituted C 1-12 alkyl chains which may contain double bonds or triple bonds; n is 1, 2, 3, 4, or 5; L is a negatively charged counter ion; and M is a positively charged counter ion. 9. The flow battery of claim 8 wherein the second redox couple includes a second organic compound, the first organic compound having a standard electrode potential that is at least 0.3 volts higher than a standard electrode potential for the second organic compound. 10. The flow battery of claim 9 wherein the first organic compound has a standard electrode potential that is at least 0.1 V positive to a mercury/mercurous sulfate electrode (MSE) for the positive electrode electrolyte. 11. The flow battery of claim 10 wherein the second organic compound has a standard electron potential at least 0.1 V negative to the MSE for the negative electrode electrolyte. 12. The flow battery of claim 10 wherein the first organic compound has an acidity greater than the acidity of the ion exchange membrane. 13. The flow battery of claim 10 wherein R 13 and R 14 are each independently —H or C 1-6 alkyl. 14. The flow battery of claim 10 wherein R 13 and R 14 are each independently —H. 15. A flow battery comprising: a positive electrode; a positive electrode electrolyte including water and a first redox couple, the positive electrode electrolyte flowing over and contacting the positive electrode, the first redox couple including a first organic compound Q 1 and a reduction product H 2 Q 1 of the first organic compound; a negative electrode; a negative electrode electrolyte including water and a second redox couple, the negative electrode electrolyte flowing over and contacting the positive electrode; and an ion exchange membrane interposed between the positive electrode and the negative electrode, wherein the first organic compound has formulae 8 and 9: wherein a and b are each independently 0, 1, 2, or 3; R 15 , R 16 , R 17 and R 18 are each independently —H, —R′, —NO 2 , —NH 2 , —N(R′R″) 2 , —N(R′R″R′″) 3 + L − , —CF 3 , —CCl 3 , —CN, —SO 3 H, —PO 3 H 2 , —COOH, —CO 2 R′, —COR′, —CHO, —OH, —OR′, —O − M + , —SO3 − M + , —PO3 − M + , —COO − M + , —CF 2 H, —CF 2 R′, —CFH3, and —CFR′R″ where R′, R″ and R′″ are alkyl or aryl groups; X is —(CH2) n , —(CH2OCH2) n , SO, SO 2 , other substituted C 1-12 alkyl chains which may contain double bonds or triple bonds; L is a negatively charged counter ion; and M is a positively charged counter ion. 16. The flow battery of claim 15 wherein the second redox couple includes a second organic compound, the first organic compound having a standard electrode potential that is at least 0.3 volts higher than a standard electrode potential for the second organic compound. 17. The flow battery of claim 16 wherein the first organic compound has a standard electrode potential that is at least 0.1 V positive to a mercury/mercurous sulfate electrode (MSE) for the positive electrode electrolyte. 18. The flow battery of claim 17 wherein the second organic compound has a standard electron potential at least 0.1 V negative to the MSE for the negative electrode electrolyte. 19. The flow battery of claim 15 wherein the first organic compound has an acidity greater than the acidity of the ion exchange membrane. 20. The flow battery of claim 15 wherein R 15 , R 16 , R 17 and R 18 are each independently —H or C 1-6 alkyl. 21. The flow battery
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