Fuel cell device
US-9225047-B2 · Dec 29, 2015 · US
US2024413363A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024413363-A1 |
| Application number | US-202218709844-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 27, 2022 |
| Priority date | Nov 23, 2021 |
| Publication date | Dec 12, 2024 |
| Grant date | — |
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Method for conditioning an electrochemical cell unit ( 53 ) before putting the electrochemical cell unit ( 53 ) into operation for converting electrochemical energy into electrical energy as a fuel cell unit ( 1 ) and/or for converting electrical energy into electrochemical energy as an electrolytic cell unit ( 49 ) having stacked electrochemical cells ( 52 ) and channels for conducting a fuel and/or an electrolyte and channels for conducting an oxidizing agent and/or an electrolyte being formed in the electrochemical cell unit ( 53 ), the method having the steps of: providing a conditioning fluid; and conducting the conditioning fluid through the channels ( 12 ) for fuel and/or electrolytes and/or conducting the conditioning fluid through the channels ( 13 ) for oxidizing agents and/or electrolytes, wherein, during at least 50% of the duration of the method for conditioning the electrochemical cell unit ( 53 ), hydrogen is conducted as the conditioning fluid through the channels ( 13 ) for oxidizing agents and/or electrolytes.
Opening claim text (preview).
1 . A method for conditioning an electrochemical cell unit ( 53 ) before putting the electrochemical cell unit ( 53 ) into operation for converting electrochemical energy into electrical energy as a fuel cell unit ( 1 ) and/or for converting electrical energy into electrochemical energy as an electrolytic cell unit ( 49 ) having stacked electrochemical cells ( 52 ) and channels ( 12 ) for conducting a fuel and/or an electrolyte and channels ( 13 ) for conducting an oxidizing agent and/or an electrolyte being formed in the electrochemical cell unit ( 53 ), the method having the steps of: providing a conditioning fluid; conducting the conditioning fluid through the channels ( 12 ) for fuel and/or electrolytes and/or conducting the conditioning fluid through the channels ( 13 ) for oxidizing agents and/or electrolytes, wherein, during at least 50% of a duration of the method for conditioning the electrochemical cell unit ( 53 ), hydrogen as the conditioning fluid is passed through the channels ( 13 ) for oxidizing agents and/or electrolytes. 2 . The method according to claim 1 , wherein hydrogen is passed through the channels ( 13 ) for oxidant and/or electrolyte during at least 70%, 80% or 90% of the duration of the method for conditioning the electrochemical cell unit ( 53 ). 3 . The method according to claim 1 , wherein hydrogen is passed through the channels ( 13 ) for oxidant and/or electrolyte during an entire duration of the method for conditioning the electrochemical cell unit ( 53 ). 4 . The method according to claim 1 , wherein during the passage of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte, anodes ( 7 ) and cathodes ( 8 ) are connected to a direct current source ( 69 ), so that a direct voltage difference is formed between the anodes ( 7 ) and cathodes ( 8 ). 5 . The method according to claim 1 , wherein during the passage of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte, protons migrate through proton exchange membranes ( 5 ) in a direction from anodes ( 7 ) to cathodes ( 8 ). 6 . The method according to claim 1 , wherein while hydrogen is passed through the channels ( 13 ) for oxidant and/or electrolyte, hydrogen is simultaneously passed through the channels ( 12 ) for fuel and/or electrolyte as conditioning fluid. 7 . The method according to claim 6 , wherein during the passage of hydrogen through the channels ( 12 ) for fuel and/or electrolyte, protons are formed from the hydrogen at anodes ( 7 ) by reducing the hydrogen to protons while releasing electrons and the protons migrate through proton exchange membranes ( 5 ) in one direction from the anodes ( 7 ) to cathodes ( 8 ). 8 . The method according to claim 1 , wherein an amount and/or mass fraction of hydrogen in the conditioning fluid which is passed through the channels ( 13 ) for oxidant and/or electrolyte and/or through the channels ( 12 ) for fuel and/or electrolyte is at least 80%, 90%, 95%, 98% or 99%. 9 . The method according to claim 1 , wherein during the passage of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte, the channels ( 12 ) for fuel and/or electrolyte are simultaneously flooded with water as conditioning fluid. 10 . The method according to claim 9 , wherein during the flooding of the channels ( 12 ) for fuel and/or electrolytes with water, protons are formed from the water at anodes ( 7 ) and the protons migrate through proton exchange membranes ( 5 ) in one direction from the anodes ( 7 ) to cathodes ( 8 ). 11 . The method according to claim 1 , wherein during the passage of hydrogen through the channels ( 13 ) for oxidizing agents and/or electrolytes, hydrogen is formed at cathodes ( 8 ) by reducing protons that have migrated through a proton exchange membrane ( 5 ) to hydrogen by accepting electrons from cathodes ( 8 ). 12 . The method according to claim 1 , wherein the hydrogen is passed through the channels ( 13 ) and/or gas chambers ( 32 ) for oxidant and/or electrolyte and/or through the channels ( 12 ) and/or gas chambers ( 31 ) for fuel and/or electrolyte with a circuit. 13 . The method according to claim 1 , wherein the hydrogen is moistened and/or enriched with water and/or water vapor before being introduced into the channels ( 13 ) for oxidant and/or electrolyte and/or into the channels ( 12 ) for fuel and/or electrolyte. 14 . The method according to claim 1 , wherein the passing of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte is carried out during a period of time between 5 min and 3 h. 15 . An electrochemical cell unit ( 53 ) for converting electrochemical energy into electrical energy as a fuel cell unit ( 2 ) and/or for converting electrical energy into electrochemical energy as an electrolysis cell unit ( 49 ), comprising stacked electrochemical cells ( 52 ) and the electrochemical cells ( 52 ) each comprise stacked layered components ( 5 , 6 , 7 , 8 , 9 , 10 , 51 ), and the components ( 5 , 6 , 7 , 8 , 9 , 10 , 51 ) of the electrochemical cells ( 52 ) are proton exchange membranes ( 5 ), anodes ( 7 ), cathodes ( 8 ), gas diffusion layers ( 9 ) and bipolar plates ( 10 , 51 ), wherein a method according to claim 1 can be carried out with the electrochemical cell unit ( 53 ). 16 . The method according to claim 12 , wherein the circuit is a common circuit. 17 . The method according to claim 14 , wherein the passing of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte is carried out during a period of time between 10 min and 2 h. 18 . The method according to claim 14 , wherein the passing of hydrogen through the channels ( 13 ) for oxidant and/or electrolyte is carried out continuously.
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