Cathode self-supporting ultra-thin solid oxide electrode and preparation method thereof
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2026-05-15
- Publication Date
- 2026-08-11
AI Technical Summary
[0006]现有技术无论是阳极支撑型电极或金属支撑型电极都会增加整体电极厚度,增加传质距离,增加会使欧姆阻抗,降低电池性能,与此同时也会使用更多的材料增加成本
[0025] The cathode self-supporting ultrathin solid oxide electrode provided by this invention greatly reduces the electrode thickness by eliminating the need for a 400-500 μm thick anode support layer or a 200-1000 μm thick metal support layer, thereby reducing mass transfer polarization and ohmic polarization, enhancing the internal heat transfer performance of the electrode, reducing start-up time, improving the uniformity of electrode heat distribution, and enhancing electrode consistency performance.
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Figure CN122552541A_ABST
Abstract
Description
Technical Field
[0001] This invention belongs to the field of solid oxide electrode technology, specifically relating to a cathode self-supporting ultrathin solid oxide electrode and its preparation method. Background Technology
[0002] Solid oxide fuel cells (SOFCs) are high-temperature fuel cells that typically operate at around 800°C. SOFCs are well-suited for the efficient and clean conversion of H2 or syngas containing hydrogen, making them an ideal alternative to traditional power generation technologies.
[0003] Traditional solid oxide fuel cell electrodes are generally classified into three types: electrolyte-supported SOFC, anode-supported SOFC, and metal-supported SOFC. Since the mechanical strength of electrolyte-supported SOFC depends on the electrolyte layer, which is typically thicker, although this provides greater mechanical strength, it also increases oxygen ion conduction resistance and overall ohmic impedance. Therefore, it is not widely used currently.
[0004] Chinese patent CN119361722A discloses a method for preparing an anode support based on cryo-casting technology. Its core innovation lies in significantly improving gas transport efficiency through unidirectional cryogenic mold design and directional pore-forming process. The specific process includes: Mold design: A special mold (outer diameter Φ5cm, cavity Φ2.5cm×3mm) is fabricated using 3D-printed ABS material. The thick-walled structure ensures that the temperature gradient is transmitted only in the vertical direction; Slurry and cryogenic process: NiO-3YSZ slurry (solid content 55wt%) is vacuum degassed and then injected into the mold, and unidirectionally frozen at -20℃ to form a vertical ice crystal template; Drying and sintering: Freeze-drying (-40℃, 36 hours) retains the directional pore structure, followed by debinding at 500℃ and sintering at 1450℃ to finally obtain an anode support with through-hole vertical channels. However, the presence of a support layer increases the electrode thickness, which is detrimental to fuel mass transfer, electron conduction, and heat transfer.
[0005] A tubular solid oxide fuel cell structure (CN111224143A) discloses a tubular solid oxide fuel cell structure, which is divided into several layers along the axial direction. Each layer contains a complete tubular fuel cell unit. Each fuel cell unit includes, from the outside to the inside, an outer shell layer, an anode electrode, an electrolyte layer, a cathode electrode, and spiral guide fins. The anode electrode includes an anode electrode support layer and an anode reaction layer, and the cathode electrode includes a cathode reaction layer and a cathode support layer. This invention can effectively enhance the mass transfer characteristics of the battery, improve the battery efficiency, and also adjust the axial distribution of battery temperature, controlling the subcooling effect of the fuel inlet section. However, this patent discloses a tubular solid oxide fuel cell and still includes a cathode support layer.
[0006] Existing technologies, whether anode-supported electrodes or metal-supported electrodes, increase the overall electrode thickness, increase the mass transfer distance, increase ohmic resistance, and reduce battery performance. At the same time, they also require more materials, increasing costs. Summary of the Invention
[0007] To address the aforementioned technical problems, this invention provides a cathode self-supporting ultrathin solid oxide electrode and its preparation method. The cathode self-supporting ultrathin solid oxide electrode significantly reduces the electrode thickness. After thinning, the heat transfer distance is shortened, optimizing the heat transfer performance, which can shorten the start-up time and enhance the consistency of current distribution.
[0008] To achieve the above objectives, the technical solution adopted by the present invention is as follows:
[0009] This invention provides a method for preparing a self-supporting ultrathin solid oxide cathode, the method comprising the following steps:
[0010] (1) Preparation of cathode functional layer: A metal support mesh or an inorganic support mesh is laid flat on the base film, and the cathode functional layer slurry is prepared on the metal support mesh or an inorganic support mesh by casting method. After drying, the cathode functional layer is formed.
[0011] (2) A barrier layer is prepared on top of the cathode functional layer;
[0012] (3) An electrolyte layer is prepared on top of the barrier layer;
[0013] (4) Prepare an anode functional layer on top of the electrolyte layer.
[0014] The metal support mesh is either Hastelloy woven mesh or Inconel nickel alloy wire mesh.
[0015] The inorganic support mesh is any one of ceramic-based support mesh, glass-based support mesh, or carbon-based support mesh.
[0016] The barrier layer is a GDC barrier layer.
[0017] The thickness of the metal support mesh or inorganic support mesh is 5~20 μm, and the mesh count is 20~3000 mesh.
[0018] The cathode functional layer slurry is composed of solvent, dispersant, cathode functional layer powder, binder, plasticizer, and pore-forming agent.
[0019] The cathode functional layer powder accounts for 25-30% of the mass percentage of the cathode functional layer slurry.
[0020] The cathode functional layer powder is LSCF powder.
[0021] The present invention also provides a cathode self-supporting ultrathin solid oxide electrode prepared by the above preparation method, wherein the cathode self-supporting ultrathin solid oxide electrode comprises, from bottom to top: a cathode functional layer, a barrier layer, an electrolyte layer, and an anode functional layer.
[0022] Furthermore, the thickness of the self-supporting ultrathin solid oxide electrode is 60~80μm.
[0023] The cathode self-supporting ultrathin solid oxide electrode provided by the present invention uses an ultrathin high-strength metal support mesh or inorganic support mesh as "steel bars" and cathode functional layer slurry as "concrete" to jointly construct the cathode functional layer. Without affecting the catalytic effect of the cathode functional layer, the electrode's mechanical properties are enhanced by the ultrathin high-strength metal support mesh or inorganic support mesh, and the cathode functional layer provides self-support.
[0024] Compared with the prior art, the present invention has the following beneficial effects:
[0025] The cathode self-supporting ultrathin solid oxide electrode provided by this invention greatly reduces the electrode thickness by eliminating the need for a 400-500 μm thick anode support layer or a 200-1000 μm thick metal support layer, thereby reducing mass transfer polarization and ohmic polarization, enhancing the internal heat transfer performance of the electrode, reducing start-up time, improving the uniformity of electrode heat distribution, and enhancing electrode consistency performance. Attached Figure Description
[0026] Figure 1 This is a schematic diagram of the cathode self-supporting ultrathin solid oxide electrode structure provided by the present invention;
[0027] Figure 2 A cross-sectional view of the anode functional layer in the cathode self-supporting ultrathin solid oxide electrode provided by the present invention;
[0028] Figure 3 A plan view of the anode functional layer in the cathode self-supporting ultrathin solid oxide electrode provided by the present invention;
[0029] Figure 4 This is a schematic diagram of the structure of a conventional anode-supported solid oxide electrode in Comparative Example 1;
[0030] Figure 5 This is a schematic diagram of the structure of a conventional metal-supported solid oxide electrode in Comparative Example 2;
[0031] Figure 6 The average thickness test diagram of the solid oxide electrode in each embodiment and comparative example;
[0032] Figure 7 The mechanical strength test diagrams of the solid oxide electrodes in each embodiment and comparative example are shown.
[0033] Figure 8 The graph shows the total conductivity of the vertical electrodes of the solid oxide electrodes in each embodiment and comparative example.
[0034] Figure 9 The in-plane conductivity test diagrams of the solid oxide electrodes in each embodiment and comparative example are shown.
[0035] Figure 10 The following are polarization curves of the solid oxide electrodes in each embodiment and comparative example. Detailed Implementation
[0036] In the description of this application, some directional terms, such as "upper", "lower", "top", "bottom", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing the embodiments of this application and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on the embodiments of this application.
[0037] The present invention provides a cathode self-supporting ultrathin solid oxide electrode, which comprises, from bottom to top, a cathode functional layer, a barrier layer, an electrolyte layer, and an anode functional layer; the cathode functional layer is obtained by casting the cathode functional layer slurry onto a metal support mesh or an inorganic support mesh and then drying it.
[0038] The thickness of the metal support mesh or inorganic support mesh is 5~20 μm, and the mesh count is 20~3000 mesh.
[0039] The metal support mesh can be selected as a high-strength metal mesh, preferably Hastelloy woven mesh or Incol nickel alloy wire mesh. The metal support mesh can be directly purchased from the market or prepared according to any method disclosed in the prior art. For example, a nickel-based metal support mesh can be prepared as follows: providing nickel-based high-temperature alloy wire, drawing it into ultra-fine wires with a diameter of less than 10μm through a multi-pass drawing process combined with intermediate annealing at 1100-1350℃, then weaving it into warp and weft, and performing micro-spot welding at the intersection of the warp and weft wires.
[0040] The inorganic support mesh can be any one of ceramic-based support mesh, glass-based support mesh, or carbon-based support mesh. Specifically, the ceramic-based support mesh can be any one of alumina ceramic, silicon carbide ceramic, silicon nitride ceramic, zirconium oxide ceramic, or high-entropy boride ceramic support mesh. The glass-based support mesh can be any one of quartz glass support mesh or borosilicate glass support mesh. The carbon-based support mesh can be any one of porous glass carbon support mesh or carbon fiber reinforced carbon support mesh. These can be directly purchased from the market or prepared according to any method disclosed in the prior art.
[0041] The cathode functional layer slurry can be any common type of cathode slurry, such as perovskite oxide slurry, specifically LSM slurry, LSCF slurry, BSCF slurry; pyrochlore oxide slurry, layered oxide slurry.
[0042] In embodiments of the present invention, the cathode functional layer slurry is preferably composed of a solvent, a dispersant, a cathode functional layer powder, a binder, a plasticizer, and a pore-forming agent.
[0043] The cathode functional layer powder accounts for 25-30% of the mass percentage of the cathode functional layer slurry.
[0044] The cathode functional layer powder is preferably LSCF powder.
[0045] The solvent is any one or more of ethanol, methanol, n-propanol, isopropanol, DMF, ethylene glycol, propylene glycol, toluene, xylene, acetone, butanone, ethyl acetate, triethanolamine, polyethylene glycol, polyvinyl butyral, and dioctyl phthalate.
[0046] The binder is any one or more of starch, polyvinyl alcohol, polyvinyl butyral, polymethyl acrylate, polymethacrylate, and ethyl cellulose.
[0047] The plasticizer is any one or more of the following: dioctyl phthalate, dibutyl phthalate, DEHP (di(2-ethylhexyl) phthalate), DBP (di-n-butyl phthalate), DINP (diisononyl phthalate), TBC (tributyl citrate), ATBC (acetylated tributyl citrate), epoxidized soybean oil (ESO), epoxidized fatty acid esters, DOA (dioctyl adipate), and DOS (dioctyl sebacate); wherein the epoxidized fatty acid ester is dioctyl tetrahydroepoxy phthalate.
[0048] The pore-forming agent is any one or more of starch, graphite, polymethyl methacrylate (PMMA), ammonium carbonate, and ammonium bicarbonate.
[0049] The anode functional layer paste can be any common type of anode paste, such as Ni-based cermet paste, specifically Ni-YSZ paste, Ni-GDC paste, Ni-SDC paste, Ni-LaGaO3-based paste; it can also be a Ni-free ceramic-based paste, such as LSCM paste, etc.
[0050] The present invention will now be described in detail with reference to the embodiments.
[0051] All percentages mentioned in the examples are mass percentages.
[0052] The Inconel nickel alloy wire mesh and high-entropy boride ceramic support mesh used in the examples are commercially available.
[0053] Example 1
[0054] A self-supporting ultrathin solid oxide electrode for cathodes comprises, from bottom to top: a cathode functional layer, a barrier layer, an electrolyte layer, and an anode functional layer; the cathode functional layer is obtained by casting the cathode functional layer slurry onto an Inconel nickel alloy wire mesh and then drying it.
[0055] The method for preparing the cathode self-supporting ultrathin solid oxide electrode includes the following steps:
[0056] S1. Preparation of cathode functional layer slurry: Under room temperature conditions, 30.12% ethanol, 12.32% nickel oxide with methyl ethyl ketone, 27% LSCF, 1.56% polyvinyl alcohol, 0.54% triethanolamine, 6.25% polyethylene glycol, 5.23% polyvinyl butyral, 14.53% dioctyl phthalate, and 2.45% polymethyl methacrylate were sequentially added to a ball mill jar and ball milled to form a stable and uniform cathode slurry. After obtaining the slurry, it was further filtered through a sieve with a pore size ≤20 μm to remove undispersed particles; then vacuum degassing was performed for 20-60 min to remove air bubbles introduced by stirring and filtration.
[0057] S2. Preparation of high-strength self-supporting cathode functional layer: A 100-mesh, 10-μm thick Inconel nickel alloy wire mesh is laid horizontally and flat on the base film. The cathode functional layer slurry is prepared onto the Inconel nickel alloy wire mesh by casting. A porous cathode functional layer is formed by gradient drying. The gradient drying process is shown in Table 1. The heating rate of each gradient is 2℃ / min. The thickness of the cathode functional layer is 19 μm.
[0058] Table 1
[0059]
[0060] S3. A GDC barrier layer is screen-printed on the above-mentioned high-strength self-supporting cathode functional layer.
[0061] S4. Preparation of electrolyte slurry: Under room temperature conditions, 26.3% YSZ, 14.2% ScCeSZ powder, 0.3% triethanolamine, 0.2% triethyl phosphate, 7.3% polyvinyl butyral, 2.8% ethyl cellulose, 1.6% dibutyl phthalate, 0.8% polyethylene glycol, 30.3% ethanol, and 16.2% methyl ethyl ketone are wet-mixed to obtain electrolyte slurry. The viscosity of the slurry is controlled at 2000-5000 mPa·s. The electrolyte slurry is then filtered and degassed to obtain electrolyte layer slurry.
[0062] S5. Electrolyte layer preparation: Electrolyte slurry is cast onto the surface of GDC barrier layer with a thickness of 14μm, and then dried and cured to obtain the electrolyte layer.
[0063] S6. Preparation of anode slurry: Under room temperature conditions, 41.21% NiO-8YSZ powder, 1.32% triethanolamine, 2.35% triethyl phosphate, 0.11% polyvinyl butyral, 0.12% ethyl cellulose, 1.27% dibutyl phthalate, 20.54% polyethylene glycol, 31.65% ethanol, and 1.43% methyl ethyl ketone are wet-mixed to obtain anode slurry. The viscosity of the slurry is controlled at 1000-5000 mPa·s. The anode slurry is then filtered and degassed to obtain the anode layer slurry.
[0064] S7. The anode slurry is prepared onto the half cell by casting. The electrode-1 is obtained by cutting, stacking, hot pressing and sintering.
[0065] Example 2
[0066] A self-supporting ultrathin solid oxide electrode for cathodes comprises, from bottom to top: a cathode functional layer, a barrier layer, an electrolyte layer, and an anode functional layer; the cathode functional layer is obtained by casting the cathode functional layer slurry onto a high-entropy boride ceramic support mesh and then drying it.
[0067] The method for preparing the cathode self-supporting ultrathin solid oxide electrode includes the following steps:
[0068] S1. Preparation of cathode functional layer slurry: Same as step S1 in Example 1.
[0069] S2. Preparation of high-strength self-supporting cathode functional layer: A high-entropy boride ceramic support mesh with a mesh size of 100 and a thickness of 8 μm is laid horizontally and flat on the base film. The cathode functional layer slurry is prepared onto the Inconel nickel alloy wire mesh by tape casting. The porous cathode functional layer is formed by gradient drying. The gradient drying process is shown in Table 1. The thickness of the cathode functional layer is 16 μm.
[0070] S3. A GDC barrier layer is screen-printed on the above-mentioned high-strength self-supporting cathode functional layer.
[0071] S4. Preparation of electrolyte slurry: Same as step S4 in Example 1;
[0072] S5. Electrolyte layer preparation: Electrolyte slurry is cast onto the surface of GDC barrier layer with a thickness of 14μm, and then dried and cured to obtain the electrolyte layer.
[0073] S6. Preparation of anode slurry: Same as step S6 in Example 1;
[0074] S7. The anode slurry is prepared onto the half cell by casting. The electrode-2 is obtained by cutting, stacking, hot pressing and sintering.
[0075] Comparative Example 1
[0076] A method for preparing an anode-supported solid oxide electrode includes the following steps:
[0077] S1. Preparation of the anode support layer: Under room temperature conditions, 49% NiO (metallic phase), 25.4% 3YSZ (ceramic skeleton), 13% ethanol, 5.5% methyl ethyl ketone (MEK), 5.5% polyvinyl butyral, 0.4% triethanolamine, and 1.2% dibutyl phthalate (DEP) were sequentially added to a ball mill jar and ball milled for 4-8 hours. Then, 5% corn starch and 1% PMMA (by mass of the above raw materials) were added, and the mixture was ball milled again for 4 hours to obtain a stable and homogeneous anode support layer slurry. After obtaining the slurry, it was filtered through a sieve with a pore size ≤20 μm to remove undispersed particles. Then, it was vacuum degassed for 20-60 minutes to remove air bubbles introduced by stirring and filtration. Finally, the anode support layer green sheet was obtained by casting, with a casting thickness of 200-500 μm, a drying temperature of 60-100℃, and a drying time of 3-12 hours.
[0078] S2. Preparation of the anode functional layer: Under room temperature conditions, 31.92% ethanol, 11.97% nickel oxide, 27.93% 8YSZ, 1.60% polyvinyl alcohol, 2.00% polyvinyl butyral, 0.24% dioctyl phthalate, 24.14% polyethylene glycol, and 0.20% polymethyl methacrylate were sequentially added to a ball mill jar and ball-milled to form a stable and uniform anode slurry. The slurry was then filtered and degassed to obtain the anode functional layer slurry. The slurry was used to prepare the anode functional layer electrode sheet by casting, and the anode functional layer was formed by gradient drying. The gradient drying process is shown in Table 1. The thickness of the anode functional layer is 10 μm.
[0079] S3. Preparation of electrolyte slurry: Same as step S4 in Example 1.
[0080] S4. Electrolyte layer preparation: Electrolyte slurry is cast onto the surface of the anode functional layer with a thickness of 14μm. After drying and curing, the scraps are cut off. After stacking the anode support layer, the glue is removed by hot pressing. The hot pressing pressure is 10-35 MPa and the sintering temperature is 800~1800℃. The half cell is obtained by cutting.
[0081] S5. Cathode functional layer construction: A GDC barrier layer is screen-printed on the above half cell, and then an LSCF cathode is screen-printed through pre-sintering. Finally, the finished electrode is obtained through co-sintering - Comparison 1.
[0082] Comparative Example 2
[0083] A method for preparing a metal-supported solid oxide electrode includes the following steps:
[0084] S1: Preparation of the metal support layer: The nickel-iron-chromium-aluminum (Ni-Fe-Cr-Al) alloy is immersed in an etchant to dissolve the non-precious metal element aluminum (Al), while retaining the nickel / iron / chromium (Ni / Fe / Cr) to form a three-dimensional through-pore structure. The etchant consists of 20 vol% H3PO4, 30 mL / L HNO3, and 50 mL / L acetic acid. It is then immersed in the electrolyte slurry from step S3 for 1-5 minutes and dried.
[0085] S2: Preparation of the anode functional layer: Under room temperature conditions, 31.92% ethanol, 11.97% nickel oxide, 27.93% 8YSZ, 1.60% polyvinyl alcohol, 2.00% polyvinyl butyral, 0.24% dioctyl phthalate, 24.14% polyethylene glycol, and 0.20% polymethyl methacrylate were sequentially added to a ball mill jar and ball-milled to form a stable and uniform anode slurry. After obtaining the slurry, it was filtered and degassed to obtain the anode functional layer slurry. The slurry was cast onto a metal support layer to obtain an anode functional layer electrode sheet, and a porous anode layer was formed by gradient drying. The gradient drying process is shown in Table 1. The thickness of the anode layer is 10 μm.
[0086] S3. Preparation of electrolyte slurry: Under room temperature conditions, 26.3% YSZ, 14.2% ScCeSZ powder, 0.3% triethanolamine, 0.2% triethyl phosphate, 7.3% polyvinyl butyral, 2.8% ethyl cellulose, 1.6% dibutyl phthalate, 0.8% polyethylene glycol, 30.3% ethanol, and 16.2% methyl ethyl ketone are wet-mixed to obtain electrolyte slurry. The viscosity of the slurry is controlled at 2000-5000 mPa·s. The electrolyte slurry is then filtered and degassed to obtain electrolyte layer slurry.
[0087] S4. Electrolyte layer preparation: Electrolyte slurry is cast onto the surface of the anode functional layer with a thickness of 14μm. After drying and curing, the scraps are cut off, and a metal support layer is stacked. The adhesive is removed by hot pressing at a pressure of 10-35 MPa and a sintering temperature of 800-1800℃. The half cell is obtained by cutting.
[0088] S5. Cathode functional layer construction: A GDC barrier layer is screen-printed on the above half cell, and then an LSCF cathode is screen-printed through pre-sintering. Finally, the finished electrode is obtained through co-sintering - Comparison 2.
[0089] Test case
[0090] The four samples were subjected to thickness testing, mechanical strength testing, thermal conductivity testing, electrical conductivity testing, and battery performance testing to characterize the physical properties and battery performance of the four samples.
[0091] The thickness test references the thickness uniformity test method in the standard "NB / T 10670-2021 Solid Oxide Fuel Cell Electrolyte Membrane Test Method Part 1: Self-Supporting Membrane" to test the sample thickness.
[0092] The mechanical strength test references section 8.2, Membrane Strength Test Method, of the standard "NB / T 10670-2021 Solid Oxide Fuel Cell Electrolyte Membrane Test Method Part 1: Self-Supporting Membrane", and tests the mechanical strength of the sample.
[0093] The conductivity test references the conductivity test method in section 9 of the standard "NB / T 10670-2021 Solid Oxide Fuel Cell Electrolyte Membrane Test Method Part 1: Self-Supporting Membrane". The electrode conductivity is tested using the four-probe test method to test the in-plane conductivity.
[0094] The thermal conductivity was tested according to the "GB T10294-2008 Determination of Steady-State Thermal Resistance and Related Properties of Thermal Insulation Materials - Protective Hot Plate Method" for testing the phase and in-plane thermal conductivity using the electrode method.
[0095] Test results are as follows Figure 6-10 As shown.
[0096] from Figure 6 As can be seen, the thickness of the solid oxide electrodes in Examples 1 and 2 decreased from 300 μm to about 70 μm compared to Comparative Examples 1 and 2, a reduction of about 76%, which is beneficial for reducing mass transfer polarization and ohmic polarization.
[0097] from Figure 7 As can be seen, although the thickness of the solid oxide electrodes in Examples 1 and 2 is significantly reduced compared to Comparative Examples 1 and 2, the mechanical strength is slightly improved. This is because the metal support mesh or inorganic support mesh adopted in this invention has high strength, which can improve the mechanical strength.
[0098] from Figure 8 As can be seen, although the thickness of the solid oxide electrodes in Examples 1 and 2 is significantly reduced compared to Comparative Examples 1 and 2, the vertical conductivity does not change much.
[0099] from Figure 9 As can be seen from the data, compared with Example 2 and Comparative Examples 1 and 2, Example 1 has a higher in-plane conductivity, which is due to the high conductivity of the Inconel alloy wire mesh.
[0100] from Figure 10As can be seen, as the current density increases from 0 to 2000 mA·cm⁻², the voltage drop of Examples 1 and 2 is smaller, and they can still maintain the voltage in the range of 0.55–0.6V at high current densities. In contrast, the voltage drop of Comparative Examples 1 and 2 is larger, especially Comparative Example 2, which has a voltage close to 0.5V at high current densities. This indicates that Examples 1 and 2 have stronger anti-polarization capabilities and can maintain a higher output voltage under high current conditions. It is evident that Examples 1 and 2 have better electrochemical performance than Comparative Examples 1 and 2.
[0101] The above detailed description of a cathode self-supporting ultrathin solid oxide electrode and its preparation method, with reference to the embodiments, is illustrative rather than limiting. Several embodiments may be listed within the defined scope. Therefore, variations and modifications without departing from the overall concept of the present invention should be within the protection scope of the present invention.
Claims
1. A method for preparing a cathode-supported ultrathin solid oxide electrode, characterized in that, The preparation method includes the following steps: (1) Preparation of cathode functional layer: A metal support mesh or an inorganic support mesh is laid flat on the base film, and the cathode functional layer slurry is prepared on the metal support mesh or an inorganic support mesh by casting method. After drying, the cathode functional layer is formed. (2) A barrier layer is prepared on top of the cathode functional layer; (3) An electrolyte layer is prepared on top of the barrier layer; (4) Prepare an anode functional layer on top of the electrolyte layer.
2. The preparation method according to claim 1, characterized in that, The metal support mesh is either Hastelloy woven mesh or Inconel nickel alloy wire mesh.
3. The preparation method according to claim 1, characterized in that, The inorganic support mesh is any one of ceramic-based support mesh, glass-based support mesh, or carbon-based support mesh.
4. The preparation method according to any one of claims 1-3, characterized in that, The barrier layer is a GDC barrier layer.
5. The preparation method according to any one of claims 1-3, characterized in that, The thickness of the metal support mesh or inorganic support mesh is 5~20 μm, and the mesh count is 20~3000 mesh.
6. The preparation method according to claim 1, characterized in that, The cathode functional layer slurry is composed of solvent, dispersant, cathode functional layer powder, binder, plasticizer, and pore-forming agent.
7. The preparation method according to claim 6, characterized in that, The cathode functional layer powder is LSCF powder.
8. The preparation method according to claim 6, characterized in that, The cathode functional layer powder accounts for 25-30% of the mass percentage of the cathode functional layer slurry.
9. The cathode self-supporting ultrathin solid oxide electrode prepared by the preparation method according to any one of claims 1-8, characterized in that, The cathode self-supporting ultrathin solid oxide electrode comprises, from bottom to top: a cathode functional layer, a barrier layer, an electrolyte layer, and an anode functional layer.
10. The cathode self-supporting ultrathin solid oxide electrode according to claim 9, characterized in that, The thickness of the self-supporting ultrathin solid oxide cathode is 60~80μm.
Citation Information
Patent Citations
Tubular solid oxide fuel cell structure
CN111224143A
Preparation method of anode support body based on freeze casting solid oxide fuel cell
CN119361722A