Fuel cell system and aircraft having an inerting system
US-2024379984-A1 · Nov 14, 2024 · US
US2024145751A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024145751-A1 |
| Application number | US-202318495412-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 26, 2023 |
| Priority date | Oct 26, 2022 |
| Publication date | May 2, 2024 |
| Grant date | — |
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According to one aspect, an electrochemical cell may include a positive electrode, a negative electrode, and an electrolyte separating the positive electrode and the negative electrode from one another. The positive electrode, the negative electrode, and the electrolyte may collectively store and discharge energy by an electrode reaction of chlorine dioxide (ClO 2 ).
Opening claim text (preview).
What is claimed is: 1 . An electrochemical cell comprising: a positive electrode; a negative electrode; and an electrolyte separating the positive electrode and the negative electrode from one, and the positive electrode, the negative electrode, and the electrolyte collectively discharging energy by an electrode reaction of chlorine dioxide (ClO 2 ). 2 . The electrochemical cell of claim 1 , wherein the electrolyte is circulatable between the positive electrode and the negative electrode. 3 . The electrochemical cell of claim 1 , wherein at least one of the positive electrode and the negative electrode is a gas diffusion electrode. 4 . The electrochemical cell of claim 1 , wherein the positive electrode has thereon a chlorite (ClO 2 − )/chlorine dioxide (ClO 2 ) couple. 5 . The electrochemical cell of claim 4 , wherein the electrolyte has a pH greater than 10. 6 . The electrochemical cell of claim 4 , wherein the positive electrode has an active layer including carbon and polytetrafluoroethylene (PTFE). 7 . The electrochemical cell of claim 6 , wherein the active layer of the positive electrode is platinum-free. 8 . The electrochemical cell of claim 4 , wherein the electrolyte includes a hydroxide, and hydroxide ion is movable between the positive electrode and the negative electrode via the electrolyte. 9 . The electrochemical cell of claim 8 , wherein the hydroxide includes lithium hydroxide (LiOH), sodium hydroxide (NaOH), potassium hydroxide (KOH), and cesium hydroxide (CsOH), or a combination thereof. 10 . The electrochemical cell of claim 8 , wherein the negative electrode has a proton/hydrogen (H 2 ) couple thereon. 11 . The electrochemical cell of claim 8 , wherein the negative electrode has an ammonia (NH 3 )/nitrogen (N 2 )/hydrogen (H 2 ) couple thereon. 12 . The electrochemical cell of claim 11 , wherein the negative electrode includes one or more platinum group metal electrocatalysts. 13 . The electrochemical cell of claim 11 , wherein the negative electrode includes one or more non-platinum group metal electrocatalysts. 14 . The electrochemical cell of claim 13 , wherein the one or more non-platinum group metal electrocatalysts includes alloys and/or intermetallic compounds, and the alloys and/or intermetallic compounds include manganese, iron, cobalt, nickel, copper, or a combination thereof. 15 . The electrochemical cell of claim 1 , wherein the positive electrode has thereon a chlorite (ClO 2 )/chlorine dioxide (ClO 2 ) couple, and the negative electrode includes aluminum. 16 . A method of operating an electrochemical cell, the method comprising: generating a voltage difference between a reaction couple on a first electrode and a chlorite/chlorine dioxide couple on a second electrode; and collecting electric current formed by ions moving, in response to the voltage difference, through an electrolyte separating the first electrode from the second electrode. 17 . The method of claim 16 , wherein the second electrode is a gas diffusion electrode, and generating the voltage difference includes supplying chlorine dioxide gas to the second electrode. 18 . The method of claim 16 , wherein the first electrode is a gas diffusion electrode, and generating the voltage difference includes supplying hydrogen or ammonia gas to the first electrode. 19 . The method of claim 16 , wherein generating the voltage difference includes removing chlorite (ClO 2 − ) from the electrochemical cell, converting the chlorite (ClO 2 − ) back to chlorine dioxide (ClO 2 ) outside of the electrochemical cell, and returning the chlorine dioxide (ClO 2 ) to the electrochemical cell. 20 . The method of claim 16 , wherein generating the voltage difference includes electrochemically producing chlorine dioxide (ClO 2 ) from chlorite (ClO 2 − ) and/or chemically producing chlorine dioxide (ClO 2 ) from one or more of chlorite (ClO 2 − ), hypochlorite (ClO − ), or hydrochloric acid (HCl).
Aluminium based · CPC title
of elements or alloys · CPC title
Alkaline electrolytes · CPC title
Metals or alloys (H01M4/92 takes precedence) · CPC title
with one metallic and one gaseous electrode · CPC title
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