Fuel cell production method
US-9496560-B2 · Nov 15, 2016 · US
US11616239B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11616239-B2 |
| Application number | US-202117563817-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 28, 2021 |
| Priority date | Dec 29, 2020 |
| Publication date | Mar 28, 2023 |
| Grant date | Mar 28, 2023 |
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Disclosed is a method for manufacturing a large-area thin-film solid oxide fuel cell, the method including: preparing an anode support slurry, an anode functional layer slurry, an electrolyte slurry, and a buffer layer slurry for tape casting; preparing an anode support green film, an anode functional layer green film, an electrolyte green film, and a buffer layer green film by tape casting the slurries onto carrier films; staking the green films, followed by hot press and warm iso-static press (WIP), to prepare a laminated body; and co-sintering the laminated body.
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What is claimed is: 1. A method for manufacturing a large-area thin-film solid oxide fuel cell, the method comprising: preparing an anode support slurry, an anode functional layer slurry, an electrolyte slurry, and a buffer layer slurry for tape casting; preparing an anode support green film, an anode functional layer green film, an electrolyte green film, and a buffer layer green film by tape casting the slurries onto carrier films; staking the green films, followed by hot press and warm iso-static press (WIP), to prepare a laminated body; and co-sintering the laminated body. 2. The method of claim 1 , wherein the anode support slurry contains, relative to the entire weight thereof, 10-14 wt % of a pore former, 8-12 wt % of a binder, 1-3 wt % of a surfactant, 1-3 wt % of a dispersion, and a plasticizer, the plasticizer to binder ratio being 0.3-0.5. 3. The method of claim 1 , wherein the anode functional layer slurry contains, relative to the entire weight thereof, 8-12 wt % of a binder, 1-3 wt % of a surfactant, 1-3 wt % of a dispersion, and a plasticizer, the plasticizer to binder ratio being 0.3-0.5. 4. The method of claim 1 , wherein the electrolyte slurry contains, relative to the entire weight thereof, 6-10 wt % of a binder, 1-3 wt % of a surfactant, 1-3 wt % of a dispersion, and a plasticizer, the plasticizer to binder ratio being 0.3-0.5. 5. The method of claim 1 , wherein the buffer layer slurry contains, relative to the entire weight thereof, 3-7 wt % of a binder, 1-3 wt % of a surfactant, 1-3 wt % of a dispersion, and a plasticizer, the plasticizer to binder ratio being 0.3-0.5. 6. The method of claim 1 , wherein the anode support layer slurry has a viscosity of 1400-1550 Cp, the anode functional layer slurry has a viscosity of 1200-1300 Cp, the electrolyte slurry has a viscosity of 300-400 Cp, and the buffer layer slurry has a viscosity of 150-250 Cp. 7. The method of claim 1 , wherein the tape casting is performed at a rate of 0.5-1 cm s −1 and a temperature of 30-70° C. 8. The method of claim 1 , wherein the hot press is performed at a pressure of 40-60 MPa and a temperature of 50-90° C. 9. The method of claim 1 , wherein, after the hot press, lamination is performed at a temperature of 40-60° C. with rotation of the green films by 90°. 10. The method of claim 1 , wherein the WIP is performed in a water/oil medium at a pressure of 40-50 MPa and a temperature of 50-90° C. 11. The method of claim 1 , wherein the co-sintering is performed at 1300-1400° C. 12. A large-area thin film solid oxide fuel cell manufactured by the method of claim 1 .
Fuel cells · CPC title
Fuel cells with solid oxide electrolytes · CPC title
Temporary supports, e.g. decal · CPC title
Sintering or firing · CPC title
characterised by the electrode/electrolyte combination or the supporting material · CPC title
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