# US 10,320,019 B2 · Process for producing a solid oxide fuel cell by depositing an electrically conductive and gas permeable layer on a porous support substrate

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- Number: US 10,320,019 B2
- Document ID: US10320019B2
- Status: Granted
- Kind: B2
- Application number: 14/618,127
- Filed: 2015-02-10
- Published: 2015-06-04
- Granted: 2019-06-11
- Earliest claimed: 2006-07-07
- Assignees: Plansee SE
- Applicants: Plansee SE
- Inventors: Karl Kailer; Georg Kunschert; Stefan Schlichtherle; Georg Strauss
- Web page: https://patentgrep.com/patent/US10320019B2

## CPC

- H01M 8/10: Fuel cells with solid electrolytes
- C23C 14/0688: {Cermets, e.g. mixtures of metal and one or more of carbides, nitrides, oxides or borides}
- C23C 14/08: Oxides (C23C14/10 takes precedence)
- C23C 14/088: {of the type ABO3 with A representing alkali, alkaline earth metal or Pb and B representing a refractory or rare earth metal}
- C23C 14/34: Sputtering
- C23C 14/3485: {using pulsed power to the target}
- H01M 4/9033: {Complex oxides, optionally doped, of the type M1MeO3, M1 being an alkaline earth metal or a rare earth, Me being a metal, e.g. perovskites}
- Y02E 60/50: Fuel cells
- Y10T 428/24997: Of metal-containing material
- Y10T 428/265: 1 mil or less
- H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- C23C: COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL (making metal-coated products by extrusion B21C23/22; covering with metal by connecting pre-existing layers to articles, see the relevant places, e.g. B21D39/00, B23K; metallising of glass C03C; metallising mortars, concrete, artificial stone, ceramics or natural stone C04B41/00; enamelling of, or applying a vitreous layer to, metals C23D; treating metal surfaces or coating of metals by electrolysis or electrophoresis C25D; single-crystal film growth C30B; by metallising textiles D06M11/83; decorating textiles by locally metallising D06Q1/04)
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y10T: TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION

## Abstract

A process for depositing an electrically conductive, preferably perovskitic layer uses a pulsed sputtering process. The layer has a low diffusivity for the elements in the iron group and is especially suitable for use in solid oxide fuel cells (SOFC). An assembly of the electrically conductive ceramic layer on a porous support substrate is also provided.

## Claims

### Claim 1

A process for producing a metal-supported solid oxide fuel cell, the process comprising the following steps:
providing a porous metallic support substrate formed of sintered grains of a Fe-based alloy, the support substrate having an open-pore structure, being gas permeable and having a density of 40% to 70% of a theoretical density;
depositing an electrically conductive ceramic diffusion barrier layer directly on the metallic porous support substrate by a pulsed sputtering process retaining the open-pore structure of the substrate and a gas permeability thereof, forming a coated porous metallic support substrate that is gas permeable; and
applying an anode in direct material contact with the coated porous support substrate to produce a support structure with an anode of the metal-supported solid oxide fuel cell.

### Claim 2 (depends on 1)

The process according to claim 1, wherein the ceramic layer has a perovskitic structure.

### Claim 3 (depends on 1)

The process according to claim 1, which further comprises using an oxide-ceramic sputtering target in the pulsed sputtering process.

### Claim 4 (depends on 1)

The process according to claim 1, which further comprises using a sputtering target in the pulsed sputtering process, wherein a concentration of elements in the sputtering target differs at most by 5% from a concentration of respective elements in the layer.

### Claim 5 (depends on 1)

The process according to claim 1, which further comprises depositing the layer at a frequency of a pulsed voltage of 1 to 1000 kHz.

### Claim 6 (depends on 5)

The process according to claim 5, which further comprises depositing the layer at a frequency of the pulsed voltage of 100 to 350 kHz.

### Claim 7 (depends on 1)

The process according to claim 1, which further comprises depositing the layer with a voltage root-mean-square value of +100 to −1000 V.

### Claim 8 (depends on 7)

The process according to claim 7, which further comprises depositing the layer with a voltage root-mean-square value of +100 to −500 V.

### Claim 9 (depends on 1)

The process according to claim 1, which further comprises depositing the layer with a mean power density of 1 to 30 W/cm2.

### Claim 10 (depends on 1)

The process according to claim 1, which further comprises using an inert gas as a process gas with a pressure of 1×10−4 to 9×10−2 mbar.

### Claim 11 (depends on 10)

The process according to claim 10, which further comprises using argon as the process gas.

### Claim 12 (depends on 1)

The process according to claim 1, wherein the layer has a structural formula ABO3, where A includes one or more elements selected from the group consisting of La, Ba, Sr and Ca; and B includes one or more elements selected from the group consisting of Cr, Mg, Al, Mn, Fe, Co, Ni, Cu and Zn.

### Claim 13 (depends on 1)

The process according to claim 1, which further comprises depositing the layer with a thickness of 0.1 to 5 μm.

### Claim 14 (depends on 1)

The process according to claim 1, which further comprises depositing the layer with a density>99% of a theoretical density.

### Claim 15 (depends on 1)

The process according to claim 1, which further comprises depositing the layer with an impurity content<0.5% by weight.

### Claim 16 (depends on 15)

The process according to claim 15, wherein the impurity content is <0.1% by weight.

### Claim 17 (depends on 1)

The process according to claim 1, wherein the porous substrate is gas permeable and the porous substrate with the conductive ceramic layer is gas permeable.
