Flow body for a gas turbine, gas turbine, method for manufacturing a flow body for a gas turbine, and method for repairing a flow body of a gas turbine
US-2024376825-A1 · Nov 14, 2024 · US
US9796021B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9796021-B2 |
| Application number | US-201514749370-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 24, 2015 |
| Priority date | Jul 23, 2010 |
| Publication date | Oct 24, 2017 |
| Grant date | Oct 24, 2017 |
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The disclosure provides a porous metal substrate structure with high gas permeability and redox stability for a SOFC and the fabrication process thereof, the porous metal substrate structure comprising: a porous metal plate composed of first metal particles; and a porous metal film composed of second metal particles and formed on the porous metal plate; wherein the porous metal plate has a thickness more than the porous metal film, and the first metal particle has a size more than the second metal particle. Further, a porous shell containing Fe is formed on the surface of each metal particle by impregnating a solution containing Fe in a high temperature sintering process of reducing or vacuum atmosphere, and the oxidation and reduction processes. The substrate uses the porous shells containing Fe particles to absorb the leakage oxygen.
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What is claimed is: 1. A method for fabricating a porous metal substrate structure to support functional layers of a solid oxide fuel cell (SOFC), comprising: providing first metal particles or a first metal slurry formed of the first metal particles, second metal particles or a second metal slurry formed of the second metal particles, a solution containing Fe and an acid solution, wherein a size of each of the first metal particles is larger than a size of each of the second metal particles; forming an un-sintered green metal plate formed of the first metal particles or the first metal slurry; forming a porous metal plate by sintering the un-sintered green metal plate; etching the porous metal plate by the acid solution to increase gas-permeability of the porous metal plate; forming an Fe impregnated porous metal plate by impregnating the solution containing Fe into the porous metal plate by a vacuum means, and then sintering the Fe impregnated porous metal plate at a temperature higher than 1100° C. in a reducing or vacuum atmosphere, until a content of Fe in the Fe impregnated porous metal plate reaches about from 6 wt % to 15 wt %; sanding the Fe impregnated porous metal plate and etching the Fe impregnated porous metal plate to clean a surface of the Fe impregnated porous metal plate and enhance permeability of the Fe impregnated porous metal plate by the acid solution; coating a porous metal film on the Fe impregnated porous metal plate to form a porous metal substrate by deposing the second metal particles on the Fe impregnated porous metal plate via a powder covering means or pasting the second metal slurry on the Fe impregnated porous metal plate, and then sintering the second metal particles or second metal slurry onto the Fe impregnated porous metal plate at a temperature higher than 1100° C. oxidizing the porous metal substrate so as to shrink pore sizes of the porous metal film; and forming porous shells containing Fe on surfaces of the first metal particles in the porous metal substrate by treating the oxidized porous metal substrate in a reduction atmosphere at a temperature higher than 700° C.. 2. The method of claim 1 , wherein the porous shells contain Ni and Fe elements, and Fe element is richer than Ni element in the porous shells. 3. The method of claim 1 , wherein the porous metal substrate is oxidized at a temperature less than 800° C. in standard atmosphere and the pore sizes of the porous metal film are shrunk to less than 35 μm. 4. The method of claim 1 , wherein the first metal particles comprise Ni and have sizes ranging from 60 μm to 250 μm. 5. The method of claim 1 , wherein each of the second metal particles comprises Ni, a Ni—Fe mixture or a Ni—Co—Fe—Cu mixture, and has a size within a range from 20 μm to 60 μm, and a content of Fe of the Ni—Fe mixture is within a range from 6 wt % to 50 wt %. 6. The method of claim 1 , wherein the first and second metal slurries are formed by respectively mixing the first and second metal particles with organic binder and solvent, wherein the organic binder and the solvent are polyvinyl alcohol and water or polyethyl cellulose and α-terpineol, respectively. 7. The method of claim 5 , the second metal particles further comprise a material selected from the group consisting of Co, Pd and Ru. 8. The method of claim 1 , wherein the step of forming the un-sintered green metal plate comprises: placing the first metal particles or the first metal slurry into a mold, and then pressing the first metal particles or the first metal slurry until the un-sintered green metal plate is formed. 9. The method of claim 1 , wherein the sintering process for forming the porous metal plate is selected from the group consisting of a vacuum sintering process, a vacuum hot-press sintering process, and a reducing atmosphere sintering process. 10. The method of claim 1 , wherein the sintering process for forming the porous metal film is selected from the group consisting of a vacuum sintering process and a reducing atmosphere sintering process. 11. The method of claim 1 , wherein the process of etching the porous metal plate by the acid solution to increase gas-permeability of the porous metal plate further comprises: etching a surface of the porous metal plate, so that the porous metal plate has a surface region that is more porous than the inside of the porous metal plate, wherein the surface region has a depth less than 150 μm and a porosity which is 1.4 to 1.8 times of the inside of the porous metal plate.
of articles with cavities or holes, not otherwise provided for in the preceding subgroups · CPC title
of flat products, e.g. sheets (B22F3/1103 takes precedence; by using pressure rollers only see B22F3/18) · CPC title
Impregnating {(making ferrous alloys by impregnation C22C33/0242)} · CPC title
Cross-Sectional Technologies · mapped topic
Fuel cells with solid oxide electrolytes · CPC title
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