Solid oxide fuel cell
US-9214693-B2 · Dec 15, 2015 · US
US9755260B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9755260-B2 |
| Application number | US-201013143539-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 6, 2010 |
| Priority date | Jan 7, 2009 |
| Publication date | Sep 5, 2017 |
| Grant date | Sep 5, 2017 |
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A method for manufacturing a high temperature electrolyzer (HTE) or a high temperature fuel cell is disclosed. According to one aspect, the HTE includes a vertical stack of n elementary planar cells alternating with n+1 interconnection plates. Each of the elementary cells include a planar porous anode and a planar porous cathode each having cutouts formed therein. The anode and cathode are respectively positioned on each of the faces of a planar dense electrolyte. Brazed joints are formed by infiltration of a defined amount of a brazing composition in the electrodes at contact points between the elementary cells and the interconnection plates.
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The invention claimed is: 1. A method of manufacturing a high temperature electrolyzer (HTE) or a high temperature fuel cell, comprising a vertical stack of n elementary planar cells alternating with n+1 interconnection plates, each of the elementary cells comprising a planar porous anode and a planar porous cathode respectively positioned on each of the faces of a planar dense electrolyte, and brazed joints being provided at contact points between the elementary cells and the interconnection plates, the method comprising the following steps: a) preparing the planar porous anode and the planar porous cathode on each face of the electrolyte, the planar porous anode being an openworked anode with through holes, and the planar porous cathode being an openworked cathode with through holes, so as to leave exposed first surface areas of each of the faces of the electrolyte corresponding to the through holes in the anode and the cathode, the exposed first surface areas delimiting second surface areas of each of the faces of the electrolyte covered by the anode or the cathode at the locations provided for the brazed joints, wherein an elementary cell is obtained comprising the openworked anode and the openworked cathode, each having a thickness; b) depositing a brazing composition layer on the surfaces of the anode and of the cathode corresponding to the second surface areas, the brazing composition amount corresponding to an amount that, in the molten state, fills the whole porosity in the thickness of the anode or of the cathode to a level corresponding to the surface of the electrolyte in the second surface areas without protruding beyond the surface of the anode or of the cathode by a thickness of more than about 20% of the thickness of the anode or of the cathode, thereby forming an elementary cell provided with a brazing composition; c) repeating the preparing and depositing n times; d) successively stacking an interconnection plate and a cell, the interconnection plate and the cell being vertically stacked; e) repeating the successive stacking n times; f) stacking an n+1 th interconnection plate; g) heating the stack formed by the elementary cells provided with the brazing composition and by the interconnection plates to a brazing temperature in order to melt the brazing composition, wherein the brazing composition fills the whole porosity in the thickness of the anode or of the cathode from their surface as far as the surface of the electrolyte in the second surface areas, without protruding beyond the surface of the anode and of the cathode by a thickness of more than about 20% of the thickness of the anode or of the cathode; h) cooling the stack from the brazing temperature to room temperature; and i) forming the electrolytes and the interconnectors with brazed joints. 2. The method according to claim 1 , wherein, in step b), the brazing composition amount is such that, in the molten state, the deposited brazing composition does not protrude beyond the surface of the anode or of the cathode; and wherein, in step g), the brazing composition does not protrude beyond the surface of the anode or of the cathode. 3. The method according to claim 1 , wherein prior to step d) a lower terminal plate of the stack is set into place on a support, and wherein following step f) a terminal upper plate of the stack is set into place. 4. The method according to claim 1 , wherein the openworked anode and the openworked cathode are prepared by selectively depositing a layer of a suspension of an anode material and a cathode material, respectively, only on said second areas of each of the faces of the electrolyte and then by sintering said layers. 5. The method according to claim 4 , further comprising: depositing a layer of suspension of a cathode material on one face of the electrolyte; sintering the deposited layer of the suspension of the cathode material; depositing a layer of a suspension of an anode material on the other face of the electrolyte; and sintering the deposited layer of the suspension of the anode material. 6. The method according to claim 1 , wherein the openworked anode and the openworked cathode are prepared by preparing a non-openworked complete anode and cathode and generating holes by removing material from the non-openworked complete anode and cathode. 7. The method according to claim 1 , wherein the brazing composition is deposited on the second surface areas by screen-printing by means of a mask, manually, or with a robot by means of a syringe and a pneumatic dispenser. 8. The method according to claim 1 , wherein the electrolyte has a thickness from about 5 to 200 μm. 9. The method according to claim 1 , wherein the electrolyte is composed of a dense material having a porosity of less than about 10% by volume. 10. The method according to claim 1 , wherein the electrolyte is a material selected from doped oxide ceramics. 11. The method according to claim 1 , wherein the anode and the cathode have a thickness from 10 to 70 μm. 12. The method according to claim 1 , wherein the anode and the cathode are in a porous material having a porosity from 30% to 50% by volume. 13. The method according to claim 1 , wherein the anode and the cathode are independently of each other composed of a material selected from the group consisting of cermet nickel-oxide—gadoliniated cerium oxide (NiO—CGO), strontiated lanthanum manganite (La 1-x Sr x Mn Y O 3-δ or LSM), the cermet: NiO-yttriated zircona YSZ, nickelates (La 4 Ni 3 O 10 , La/Nd 2 NiO 4 ), chromo-manganites (LaCeSrCrMnO), ferrites (La 1-X Sr X Fe Y O 3-δ ), cobaltites (La 1-X Sr X Co Y O 3-δ ) and titanates (La 4 Sr n-4 Ti n O 3n+2-δ ). 14. The method according to claim 1 , wherein step g) is carried out in air. 15. The method according to claim 1 , wherein the anode, the cathode and the electrolyte have identical planar surfaces. 16. The method according to claim 6 , wherein the openworked anode and the openworked cathode are prepared by preparing a non-openworked complete anode and cathode by screen-printing followed by sintering, and by generating holes by removing material from the non-openworked complete anode and cathode by laser ablation or machining. 17. The method according to claim 1 , wherein the electrolyte has a thickness from about 50 to 150 μm. 18. The method according to claim 1 , wherein the electrolyte has a thickness of about 90 μm. 19. The method according to claim 1 , wherein the anode and the cathode have a thickness of about 40 μm. 20. The method according to claim 1 , wherein the anode, the cathode and the electrolyte have identical planar surfaces which coincide. 21. The method according to claim 4 , wherein the layer of the suspension of the anode material and the layer of the suspension of the cathode material are each deposited by screen-printing by use of a mask. 22. The method according to claim 1 , wherein the through holes pass through a stack of elementary cells and interconnecting plates. 23. The method according to claim 1 wherein the through holes are annular holes. 24. The method according to claim 10 , wherein the doped oxide ceramic is selected from the group consisting of yttriated zirconia, scandiated zirconia and strontiated lanthanum manganite doped with cerium.
Fuel cells with solid oxide electrolytes · CPC title
Details (electrodes H01M4/86 - H01M4/98) · CPC title
characterised by the electrode/electrolyte combination or the supporting material · CPC title
Porous electrodes · CPC title
the electrolyte consisting of oxides · CPC title
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