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Solid oxide fuel battery anode and its production

A solid oxide, fuel cell technology, applied in the direction of battery electrodes, circuits, electrical components, etc., can solve problems such as peeling or falling off, electrode performance degradation, high catalytic activity, etc., to achieve chemical and structural stability, structural size stability, and catalytic activity high effect

Inactive Publication Date: 2009-01-21
UNIV OF SCI & TECH OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The British "Natural Materials" magazine ("Nature Materials", vol.3, 2004, 17-27) pointed out that: cermet anodes for solid oxidation fuel cells, such as Ni-YSZ, Ni-DCO, Cu-YSZ, Cu-DCO, Cu / Ni alloy-YSZ, Cu / Ni alloy-DCO, etc. (YSZ is Y 2 o 3 doped stabilized ZrO 2 Electrolyte, DCO is doped CeO 2 Electrolyte), using hydrogen as fuel, has good electrode performance, but operating with hydrocarbons as fuel, there are many problems: 1) Because the catalytic activity of Ni is too high, it is easy to cause carbon deposition on the anode and electrode performance decline or completely lose Function; 2) Poor oxidation-reduction resistance: the metal in the cermet anode is easy to oxidize, and the generated oxide often has a large volume change
Therefore, during the anodic oxidation-reduction cycle, severe mechanical stress is prone to occur inside the electrode, causing the anode to crack or peel or fall off from the electrolyte layer; 3) poor sulfur resistance, while many hydrocarbon fuels in existing fuel systems All contain sulfide more or less; 4) Long-term high-temperature operation, the dispersed metal phase in the cermet anode is agglomerated, resulting in a serious decline in electrode performance
The article also pointed out that the use of doped perovskite-type lanthanum chromate and titanate single-phase composite oxide anodes, although the problems of carbon deposition on the anode and matching with adjacent materials have been solved, the fuel oxidation catalytic activity of the electrode still needs to be improved

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Prepared with porous La 0.7 Sr 0.3 CrO 3 As the structural skeleton of the anode and the main electronic conductor, the nanoparticle SDC (SDC=Ce 0.8 SM 0.2 o 1.9 ) surface modified porous support anode.

[0016] Proceed as follows:

[0017] 1) with La 2 o 3 , SrCO 3 , Cr 2 o 3 As a raw material, La was prepared by a solid-state reaction method 0.7 Sr 0.3 CrO 3 Powder. Namely: put La 2 o 3 , SrCO 3 , Cr 2 o 3 Press La 0.7 Sr 0.3 CrO 3 Grinding and mixing the proportions of the various metal elements in the formula, then pressing into tablets or blocks, and burning at 1300°C for 10 hours; then crushing and grinding the burned pieces or blocks, and then pressing into tablets or blocks, and then crushing and grinding to obtain d 50 = 12 µm La 0.7 Sr 0.3 CrO 3 Powder.

[0018] 2) Using water as a solvent, adding La with a mass ratio of 60% 0.7 Sr 0.3 CrO 3 , 3% methyl cellulose as a binder, 7% starch pore-forming agent, 0.3% polyacrylic acid disp...

Embodiment 2

[0029] Prepared with porous La 0.7 Ca 0.3 Cr 0.5 mn 0.5 o 3 It is the structural skeleton and electronically conductive phase of the anode, and the surface is modified with a porous support anode of nanoparticle Ni-GDC film. The mass content of Ni in Ni-GDC is 5%, GDC=Ce 0.8 Gd 0.2 o 1.9 .

[0030] Proceed as follows:

[0031] 1) with La 2 o 3 , CaCO 3 , MnO 2 , Cr 2 o 3 For raw material, adopt La in embodiment 1 0.7 Sr 0.3 CrO 3 A similar solid phase reaction method was used to prepare La 0.7 Ca 0.3 Cr 0.5 mn 0.5 o 3 Powder;

[0032] 2) Adopt organic polymer dispersant (polyacrylic acid, molecular weight is 5000, add-on is 0.7% of solid powder quality), methyl cellulose (add-on is 6% of solid powder quality) binding agent, prepare La 0.7 Ca 0.3 Cr 0.5 mn 0.5 o 3 Water-based slurry, tape casting (table casting) to prepare La 0.7 Ca 0.3 Cr 0.5 mn 0.5 o 3 The green body (plate) is sintered at 1600°C for 4 hours after drying to obtain a porous La wi...

Embodiment 3

[0038] Prepared with porous Sr 0.86 Y 0.1 TiO 3 It is the skeleton of the anode structure and the main electronic conductor, and the surface is loaded with Ni-YSZ 96vol% of nanoparticles (YSZ=Zr 0.8 Y 0.2 o 1.9 ) anode.

[0039] Proceed as follows:

[0040] 1) with TiO 2 and SrCO 3 , Y 2 o 3 As raw material, Sr was prepared by solid state reaction method 0.86 Y 0.1 TiO 3 Powder;

[0041] 2) Add 0.5% of the split mass as a dispersant, 4% of methyl cellulose binder, etc., to prepare Sr 0.86 Y 0.1 TiO 3 Water-based slurry, followed by table casting to prepare Sr 0.86 Y 0.1 TiO 3 Green body, after drying, sintering at 1600°C for 4 hours to obtain Sr with a porosity of about 34% 0.86 Y 0.1 TiO 3 Porous ceramic body;

[0042] 3) Nickel nitrate (Ni(NO) 2 ), yttrium nitrate (Y(NO) 3 ) and zirconium oxychloride (ZrOCl 2 ·8H 2 O)) as raw material, prepare a mixed aqueous solution with a concentration of about 0.01M, Ni 2+ , Y 3+ , Zr 4+ The ratio meets Ni-YS...

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Abstract

A solid oxide fuel battery anode and the preparation method, the characteristic is: adulterates the titanic mine cadmium acid lanthanum or the titanate compound oxide as the anode structure framework and the main electron conducting phase, uses the ion infusing method, the macromolecule modeling board method, the sol-gel method, or the suspending grain pulp spreading method, prepares the nanometer grain anode active substance multi-hole film with the thickness of 0.05-5 micron in the inner and outer hole surface of the multi-hole anode structure framework; the anode active substance includes the ceric oxide, or the adulterating ceric oxide, or the zirconia based oxygen ionic conductor electrolyte, or the cerate based proton conductor electrolyte, or the mixture of the above active substance, or the above active substance adding a small quantity of Ni or Ni-Cu and V2O5. The invention is structure stabilization, high conducting rate, high catalyzing activity of the fuel oxidation, matching with the closing material at physics and chemistry, structure size stabilization, anti-carbon deposition, is fit for the fuel operation of the hydrocarbon directly.

Description

Technical field: [0001] The invention belongs to the technical field of fuel cells, in particular to an anode material of a solid oxide fuel cell directly fueled by hydrocarbons and an anode preparation method. Background technique: [0002] The British "Natural Materials" magazine ("Nature Materials", vol.3, 2004, 17-27) pointed out that: cermet anodes for solid oxidation fuel cells, such as Ni-YSZ, Ni-DCO, Cu-YSZ, Cu-DCO, Cu / Ni alloy-YSZ, Cu / Ni alloy-DCO, etc. (YSZ is Y 2 o 3 doped stabilized ZrO 2 Electrolyte, DCO is doped CeO 2 Electrolyte), using hydrogen as fuel, has good electrode performance, but operating with hydrocarbons as fuel, there are many problems: 1) Because the catalytic activity of Ni is too high, it is easy to cause carbon deposition on the anode and electrode performance decline or completely lose Function; 2) Poor oxidation-reduction resistance: the metal in the cermet anode is easy to oxidize, and the generated oxide often has a large volume chang...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): H01M4/86H01M4/88
CPCY02E60/50
Inventor 高建峰孟广耀
Owner UNIV OF SCI & TECH OF CHINA
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