IP Library Granted Patent US 7,141,271
Granted Patent B2
US 7,141,271 · App. 10/362,831 · Granted Nov 28, 2006

Method for producing a solid ceramic fuel cell

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Quick Facts
Patent No.
US 7,141,271
App. No.
10/362,831
Granted
Nov 28, 2006
Kind
B2
Abstract

According to a method for producing a solid ceramic fuel cell, a solid electrolyte layer is gas-tightly deposited on an electrode inside a coating chamber, using a plasma spraying technique. The pressure inside the coating chamber is set at less than approximately 15 mbar for this purpose. A coating material is powder form, preferably with a particle diameter of significantly less than 10 μm, is finely dispersed in the plasma jet in such a way that the individual particles are isolated from each other when they meet the electrode. This enables a very homogenous and impervious solid electrolyte layer to be deposited.

Claims (28)

1. A process for producing a solid oxide fuel cell, including a solid electrolyte layer arranged between two porous electrodes, comprising:

applying the solid electrolyte layer in gastight form to one of the electrodes via a plasma-spraying process in a coating chamber in which the pressure is less than 15 mbar, wherein individual particles of a coating material are entrained in a plasma jet, and wherein the particles are thinly distributed in the plasma jet in such a manner that they are applied to the one of the electrodes in substantially isolated form.

2. The process as claimed in claim 1 , further comprising:

producing a continuous layer after the plasma jet has passed over the electrode a plurality of times.

3. The process as claimed in claim 2 , wherein the layer is continuous after the plasma jet has passed over the electrode about 20 to 60 times.

4. The process as claimed in claim 1 , wherein the total layer thickness of the solid electrolyte layer is between 5 μm and 30 μm.

5. The process as claimed in claim 1 , wherein the plasma jet on the electrode includes a jet diameter of between 30 and 50 cm.

6. The process as claimed in claim 1 , wherein a pulverulent coating material with a mean particle diameter of less than 20 μm is introduced into the plasma jet.

7. The process as claimed in claim 1 , wherein the leak rate of the solid electrolyte layer is less than 10*10 −4 mbar l/sec/cm 2 .

8. The process as claimed in claim 1 , wherein the density of the coating is set by varying the process parameters.

9. The process as claimed in claim 8 , wherein the density is set by selecting the mean particle size.

10. The process as claimed in claim 1 , further comprising: applying an interconnector as a further layer via the plasma-spraying process.

11. The process as claimed in claim 1 , wherein at least one of the electrodes is produced via the plasma-spraying process.

12. The process as claimed in claim 1 , wherein the process parameters are varied during the coating.

13. The process as claimed in claim 1 , wherein the fuel cell is designed as a tubular hollow body.

14. The process as claimed in claim 3 , wherein the layer has a layer thickness of 5 μm to 10 μm.

15. The process as claimed in claim 1 , wherein the total layer thickness of the solid electrolyte layer is between 5 μm and 30 μm.

16. The process as claimed in claim 1 , wherein the total layer thickness of the solid electrolyte layer is between 5 μm and 30 μm.

17. The process as claimed in claim 4 , wherein the plasma jet on the electrode includes a jet diameter of 40 cm.

18. The process as claimed in claim 2 , wherein the plasma jet on the electrode includes a jet diameter of between 30 and 50 cm.

19. The process as claimed in claim 3 , wherein the plasma jet on the electrode includes a jet diameter of between 30 and 50 cm.

20. The process as claimed in claim 1 , wherein a pulverulent coating material with a mean particle diameter of less than 10 μm is introduced into the plasma jet.

21. The process as claimed in claim 1 , wherein the leak rate of the solid electrolyte layer is less than 2.3*10 −4 mbar l/sec/cm 2 .

22. A method for producing a solid oxide fuel cell, including a solid electrolyte layer arranged between two porous electrodes, comprising:

applying the solid electrolyte layer in gastight form to one of the electrodes via a plasma-spraying process in a coating chamber in which the pressure is less than 15 mbar, wherein particles of a coating material are dispersed in the plasma jet in such a manner that they are applied to the one of the electrodes in substantially isolated form.

23. The process as claimed in claim 22 , further comprising:

producing a continuous layer by passing the plasma jet over the at least one electrode a plurality of times.

24. The process as claimed in claim 23 , wherein the layer is continuous after the plasma jet has passed over the electrode about 20 to 60 times.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 14, 2012
From: SIEMENS ENERGY, INC.
To: SIEMENS AKTIENGESELLSCHAFT
Reel/Frame 029124/0628 →
IP ASSIGNMENT AND LICENSE AGREEMENT Recorded Mar 15, 2010
From: SIEMENS AKTIENGESELLSCHAFT
To: SIEMENS ENERGY, INC.
Reel/Frame 024066/0878 →
CHANGE OF NAME Recorded Sep 15, 2005
From: SIEMENS WESTINGHOUSE POWER CORPORATION
To: SIEMENS POWER GENERATION, INC.
Reel/Frame 017000/0120 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 5, 2003
From: BARBEZAT, GERARD; FLECK, ROBERT; JANSING, THOMAS; LOCH, MICHAEL
To: SIEMENS AKTIENGESELLSCHAFT SULZER METCO AG
Reel/Frame 014353/0316 →