CN114016063B - A kind of solid oxide electrolytic cell and preparation method thereof - Google Patents
A kind of solid oxide electrolytic cell and preparation method thereof Download PDFInfo
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- 239000007787 solid Substances 0.000 title claims abstract description 23
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 239000010410 layer Substances 0.000 claims abstract description 106
- 239000001257 hydrogen Substances 0.000 claims abstract description 65
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 65
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 239000001301 oxygen Substances 0.000 claims abstract description 50
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 50
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000003792 electrolyte Substances 0.000 claims abstract description 45
- 239000011229 interlayer Substances 0.000 claims abstract description 34
- 230000000903 blocking effect Effects 0.000 claims abstract description 32
- 229910000420 cerium oxide Inorganic materials 0.000 claims abstract description 25
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 claims abstract description 25
- 229910052772 Samarium Inorganic materials 0.000 claims abstract description 13
- 229910052746 lanthanum Inorganic materials 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 11
- 229910052727 yttrium Inorganic materials 0.000 claims abstract description 9
- 239000002131 composite material Substances 0.000 claims abstract description 8
- 230000004888 barrier function Effects 0.000 claims abstract description 6
- 238000004544 sputter deposition Methods 0.000 claims description 24
- 239000011267 electrode slurry Substances 0.000 claims description 17
- 239000000843 powder Substances 0.000 claims description 16
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 15
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 12
- 238000001755 magnetron sputter deposition Methods 0.000 claims description 12
- 229910052688 Gadolinium Inorganic materials 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 11
- 238000007650 screen-printing Methods 0.000 claims description 11
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 10
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 10
- 235000021323 fish oil Nutrition 0.000 claims description 10
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 10
- 239000001856 Ethyl cellulose Substances 0.000 claims description 6
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 claims description 6
- WUOACPNHFRMFPN-UHFFFAOYSA-N alpha-terpineol Chemical compound CC1=CCC(C(C)(C)O)CC1 WUOACPNHFRMFPN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052786 argon Inorganic materials 0.000 claims description 6
- SQIFACVGCPWBQZ-UHFFFAOYSA-N delta-terpineol Natural products CC(C)(O)C1CCC(=C)CC1 SQIFACVGCPWBQZ-UHFFFAOYSA-N 0.000 claims description 6
- 229920001249 ethyl cellulose Polymers 0.000 claims description 6
- 235000019325 ethyl cellulose Nutrition 0.000 claims description 6
- 239000000758 substrate Substances 0.000 claims description 6
- 229940116411 terpineol Drugs 0.000 claims description 6
- 239000002202 Polyethylene glycol Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 229920001223 polyethylene glycol Polymers 0.000 claims description 5
- 239000002994 raw material Substances 0.000 claims description 5
- -1 (Sm Inorganic materials 0.000 claims description 4
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 claims description 4
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 229910052769 Ytterbium Inorganic materials 0.000 claims description 2
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 claims description 2
- 229910018921 CoO 3 Inorganic materials 0.000 claims 3
- 239000011248 coating agent Substances 0.000 claims 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 claims 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims 2
- 229910003026 (La,Sr)(Co,Fe)O3 Inorganic materials 0.000 claims 1
- 229910052742 iron Inorganic materials 0.000 claims 1
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 4
- 238000005868 electrolysis reaction Methods 0.000 abstract description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 2
- 239000001569 carbon dioxide Substances 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 229910052691 Erbium Inorganic materials 0.000 abstract 2
- 229910002127 La0.6Sr0.4Co0.2Fe0.8O3 Inorganic materials 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- 239000000446 fuel Substances 0.000 description 4
- 210000001161 mammalian embryo Anatomy 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Substances C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical group [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229910004625 Ce—Zr Inorganic materials 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 239000002001 electrolyte material Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 125000006850 spacer group Chemical group 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/60—Constructional parts of cells
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
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Abstract
Description
技术领域technical field
本发明涉及燃料电池及电解池领域,具体涉及一种固体氧化物电解池及其制备方法。The invention relates to the field of fuel cells and electrolytic cells, in particular to a solid oxide electrolytic cell and a preparation method thereof.
背景技术Background technique
固体氧化物电解池(Solid Oxide electrolysis Cell,简称SOEC)可看作固体氧化物燃料电池的逆过程,可在高温下将水蒸气电解为氢气和氧气,或供电解水蒸气和二氧化碳为合成气,其表观电效率可达到100%,目前被认为是最高效的电解制氢技术。Solid Oxide Electrolysis Cell (SOEC) can be regarded as the reverse process of solid oxide fuel cell, which can electrolyze water vapor into hydrogen and oxygen at high temperature, or electrolyze water vapor and carbon dioxide into synthesis gas. Its apparent electrical efficiency can reach 100%, and it is currently considered to be the most efficient electrolytic hydrogen production technology.
高成本是阻碍固体氧化物燃料电池或电解池商业化应用的重要原因。为了降低成本,固体氧化物燃料电池或电解池低温化已成为本领域的研究热点。膜电极是SOEC的核心部件,其具有“三明治”结构,中间是致密的电解质层,两边为多孔的氢电极和氧电极。电解质层的欧姆电阻通常是占据整个膜电极电阻的主要部分。目前,掺杂的氧化锆材料是常用的SOEC电解质材料,但其低温下氧离子电导率低,导致电池性能显著下降。掺杂的氧化铈材料在低温下具有更高的氧离子电导率,但其存在一定的电子电导率,导致电池的开路电位(OCV)低于理论值,降低电池效率。High cost is an important reason hindering the commercial application of solid oxide fuel cells or electrolytic cells. In order to reduce the cost, the low temperature of solid oxide fuel cells or electrolytic cells has become a research hotspot in this field. Membrane electrode is the core component of SOEC, which has a "sandwich" structure with a dense electrolyte layer in the middle and porous hydrogen and oxygen electrodes on both sides. The ohmic resistance of the electrolyte layer usually occupies the main part of the entire membrane electrode resistance. At present, doped zirconia materials are commonly used as SOEC electrolyte materials, but their low oxygen ion conductivity at low temperatures leads to a significant decrease in battery performance. The doped cerium oxide material has higher oxygen ion conductivity at low temperature, but it has a certain electronic conductivity, which causes the open circuit potential (OCV) of the battery to be lower than the theoretical value and reduces the battery efficiency.
发明内容Contents of the invention
基于以上的背景技术,本发明提出一种低温固体氧化物电解池及其制备方法,该电解池基于掺杂氧化铈基电解质,在低温下具有较低的欧姆电阻并具有较高的OCV,实现了优异的性能输出。具体如下:Based on the above background technology, the present invention proposes a low-temperature solid oxide electrolytic cell and its preparation method. The electrolytic cell is based on a doped cerium oxide-based electrolyte, which has a lower ohmic resistance and a higher OCV at low temperatures, and realizes excellent performance output. details as follows:
一种低温固体氧化物电解池,所述电解池包括氢电极层、电解质层、电子阻挡层、隔层、氧电极层,其中,氢电极层为NiO与掺杂的氧化铈LnxCe1-xO2组成的复合材料,NiO与LnxCe1-xO2的质量比为40∶60~70∶30,氢电极层厚度为500-2000纳米,孔隙率为30~60%,氢电极层中,Ln为La、Gd、Sm、Pr、Er中的一种或多种,0.1≤x≤0.5;电解质层为掺杂的氧化铈(LnxCe1-xO2),Ln为La、Gd、Sm、Pr、Er中的一种或多种,0.1≤x≤0.5,电解质层厚度为2~20微米,电子阻挡层为掺杂的氧化锆基材料(MyZr1-yO2),M为Y、Sc、Ce、Yb、La、Gd、Sm中的一种或几种,0≤y≤0.5,电子阻挡层为2~500纳米,隔层为掺杂的氧化铈(LnxCe1-xO2),Ln为La、Gd、Sm、Y、Pr、Er中的一种或多种,0.1≤x≤0.5,隔层厚度为0.2~5微米,氧电极为钙钛矿氧化物、类钙钛矿氧化物或钙钛矿氧化物与掺杂的氧化铈或类钙钛矿氧化物与掺杂的氧化铈构成的复合材料,钙钛矿氧化物与掺杂的氧化铈的质量比为50∶50~80∶20,类钙钛矿氧化物与掺杂的氧化铈的质量比为50∶50~80∶20,氧电极层厚度为10~100微米,氧电极层孔隙率为30~60%。A low-temperature solid oxide electrolytic cell, the electrolytic cell includes a hydrogen electrode layer, an electrolyte layer, an electron blocking layer, an interlayer, and an oxygen electrode layer, wherein the hydrogen electrode layer is NiO and doped cerium oxide Ln x Ce 1- The composite material composed of x O 2 , the mass ratio of NiO to Ln x Ce 1-x O 2 is 40:60-70:30, the thickness of the hydrogen electrode layer is 500-2000 nanometers, the porosity is 30-60%, the hydrogen electrode In the layer, Ln is one or more of La, Gd, Sm, Pr, Er, 0.1≤x≤0.5; the electrolyte layer is doped cerium oxide (Ln x Ce 1-x O 2 ), Ln is La , Gd, Sm, Pr, Er, one or more, 0.1≤x≤0.5, the thickness of the electrolyte layer is 2-20 microns, and the electron blocking layer is a doped zirconia-based material (M y Zr 1-y O 2 ), M is one or more of Y, Sc, Ce, Yb, La, Gd, Sm, 0≤y≤0.5, the electron blocking layer is 2-500 nanometers, and the interlayer is doped cerium oxide ( Ln x Ce 1-x O 2 ), Ln is one or more of La, Gd, Sm, Y, Pr, Er, 0.1≤x≤0.5, the thickness of the interlayer is 0.2-5 microns, and the oxygen electrode is calcium Composite materials composed of titanium oxide, perovskite-like oxide or perovskite oxide and doped cerium oxide or perovskite-like oxide and doped cerium oxide, perovskite oxide and doped The mass ratio of cerium oxide is 50:50 to 80:20, the mass ratio of perovskite-like oxide to doped cerium oxide is 50:50 to 80:20, and the thickness of the oxygen electrode layer is 10 to 100 microns. The layer porosity is 30-60%.
进一步地,在上述技术方案中,所述氢电极厚优选为800~1500纳米,孔隙率优选为40~55%。Further, in the above technical solution, the thickness of the hydrogen electrode is preferably 800-1500 nanometers, and the porosity is preferably 40-55%.
进一步地,在上述技术方案中,所述电解质层为掺杂的氧化铈(LnxCe1-xO2),Ln优选Gd、Sm、Pr、Er中的一种或多种,电解质层厚度优选为5~10微米。Further, in the above technical solution, the electrolyte layer is doped cerium oxide (Ln x Ce 1-x O 2 ), Ln is preferably one or more of Gd, Sm, Pr, Er, and the thickness of the electrolyte layer is Preferably it is 5-10 microns.
进一步地,在上述技术方案中,所述电子阻挡层为掺杂的氧化锆基材料(MyZr1- yO2),M优选为Y、La、Gd、Sm中的一种或几种,电子阻挡层优选为5~50纳米。Further, in the above technical solution, the electron blocking layer is a doped zirconia-based material (M y Zr 1- y O 2 ), M is preferably one or more of Y, La, Gd, Sm , the electron blocking layer is preferably 5-50 nanometers.
进一步地,在上述技术方案中,所述隔层为掺杂的氧化铈(LnxCe1-xO2),Ln优选为La、Gd、Sm、Pr、Er中的一种或多种,隔层厚度优选为0.2~2微米。Further, in the above technical solution, the interlayer is doped cerium oxide (Ln x Ce 1-x O 2 ), Ln is preferably one or more of La, Gd, Sm, Pr, Er, The thickness of the interlayer is preferably 0.2-2 microns.
进一步地,在上述技术方案中所述氧电极优选为钙钛矿氧化物与掺杂的氧化铈或类钙钛矿氧化物与掺杂的氧化铈构成的复合材料,氧电极层厚度优选为20~50微米,氧电极层孔隙率优选为40~55%。Further, in the above technical solution, the oxygen electrode is preferably a composite material composed of perovskite oxide and doped cerium oxide or a perovskite-like oxide and doped cerium oxide, and the thickness of the oxygen electrode layer is preferably 20 The porosity of the oxygen electrode layer is preferably 40-55%.
本发明提供上述电解池制备方法,过程如下,(1)将NiO与掺杂的氧化铈(LnxCe1- xO2)按照一定质量比混合研磨5~50h后形成氢电极粉体,将氢电极粉体、甲苯、乙醇、鱼油、聚乙二醇、邻苯二甲酸二辛酯和聚乙烯醇缩丁醛混合球磨10~100h形成氢电极浆料,上述原料比例为:100∶60~100∶20~50∶1~5∶3~6∶3~6∶6~10,将氢电极浆料流延成型后形成氢电极生胚,将生胚干燥后在高温炉中800~1200℃预烧2~20h,形成氢电极支撑体;(2)将电解质粉体与正丁醇、邻苯、聚乙烯醇缩丁醛、鱼油混合研磨10~100h形成电解质浆料,上述原料比例为:100∶200~300∶10~40∶10~40∶1~5,采用丝网印刷或直接涂覆法将电解质浆料制备到氢电极支撑体,在高温1300~1500℃烧结2~20h;(3)采用磁控溅射法制备电子阻挡层,在200~600℃退火处理;(4)采用磁控溅射法在电子阻挡层上制备隔层,在800~1100℃退火处理;(5)将氧电极粉体与松油醇、乙基纤维素混合研磨2~50h形成氧电极浆料,采用丝网印刷或直接涂覆法将氧电极浆料制备到隔层上,在高温800~1200℃烧结2~10h,得到全电池。The invention provides the preparation method of the above-mentioned electrolytic cell, the process is as follows: (1) NiO and doped cerium oxide (Ln x Ce 1- x O 2 ) are mixed and ground according to a certain mass ratio for 5-50 hours to form a hydrogen electrode powder, and Hydrogen electrode powder, toluene, ethanol, fish oil, polyethylene glycol, dioctyl phthalate and polyvinyl butyral are mixed and ball milled for 10-100 hours to form a hydrogen electrode slurry. The ratio of the above raw materials is: 100:60~ 100: 20-50: 1-5: 3-6: 3-6: 6-10, the hydrogen electrode slurry is tape-cast to form a hydrogen electrode green body, and the green body is dried in a high-temperature furnace at 800-1200°C Pre-fire for 2-20 hours to form a hydrogen electrode support; (2) Mix and grind the electrolyte powder with n-butanol, o-benzene, polyvinyl butyral, and fish oil for 10-100 hours to form an electrolyte slurry. The ratio of the above raw materials is: 100: 200-300: 10-40: 10-40: 1-5, the electrolyte slurry is prepared on the hydrogen electrode support by screen printing or direct coating method, and sintered at a high temperature of 1300-1500 °C for 2-20 hours; ( 3) Prepare the electron blocking layer by magnetron sputtering, and anneal at 200-600°C; (4) Prepare an interlayer on the electron-blocking layer by magnetron sputtering, and anneal at 800-1100°C; (5) Mix and grind the oxygen electrode powder with terpineol and ethyl cellulose for 2 to 50 hours to form an oxygen electrode slurry, and prepare the oxygen electrode slurry on the interlayer by screen printing or direct coating method, at a high temperature of 800 to 1200 ℃ sintering for 2 to 10 hours to obtain a full battery.
进一步地,在上述技术方案中采用磁控溅射法制备电子阻挡层,溅射气氛为氧气和氩气混合气,两者流量比为1/1~1/40,溅射基底温度为100~400℃,溅射气压为0.1Pa~3.5Pa,溅射功率密度P=3~35Wcm-2。Further, in the above technical solution, the magnetron sputtering method is used to prepare the electron blocking layer, the sputtering atmosphere is a mixed gas of oxygen and argon, the flow ratio of the two is 1/1 to 1/40, and the sputtering substrate temperature is 100 to 1/40. 400°C, sputtering pressure is 0.1Pa-3.5Pa, sputtering power density P=3-35Wcm -2 .
进一步地,在上述技术方案中采用磁控溅射法制备隔层,溅射气氛为氧气和氩气混合气,两者流量比为1/1~1/20,溅射基底温度为100~600℃,溅射气压为0.1Pa~2Pa,溅射功率密度p=3~20Wcm-2。Further, in the above technical solution, the magnetron sputtering method is used to prepare the interlayer, the sputtering atmosphere is a mixture of oxygen and argon, the flow ratio of the two is 1/1 to 1/20, and the sputtering substrate temperature is 100 to 600 °C, the sputtering pressure is 0.1Pa-2Pa, and the sputtering power density is p=3-20Wcm -2 .
发明有益效果Beneficial effect of the invention
(1)本发明基于氧化铈基电解质,在掺杂氧化铈基电解质表面制备了电子阻挡层MyZr1-yO2和隔层LnxCe1-xO2,电子阻挡层MyZr1-yO2有效地抑制了掺杂氧化铈的内漏电问题,隔层则避免了电子阻挡层与高活性Co/Fe基钙钛矿基氧电极高温下发生有害反应。应用于固体氧化物电解池,可用于电解水制氢,且电解池运行可靠性。(1) The present invention is based on a ceria-based electrolyte, and an electron blocking layer My Zr 1-y O 2 and a spacer layer Ln x Ce 1-x O 2 are prepared on the surface of a doped ceria-based electrolyte. The electron blocking layer My Zr The 1-y O2 effectively suppresses the internal leakage problem of doped ceria, and the interlayer avoids the harmful reaction between the electron blocking layer and the highly active Co/Fe-based perovskite-based oxygen electrode at high temperature. Applied to solid oxide electrolytic cells, it can be used to electrolyze water to produce hydrogen, and the operation of electrolytic cells is reliable.
(2)本发明采用磁控溅射方法制备电子阻挡层和隔层,电子阻挡层与隔层的均一性更好,且避免了高温烧结的过程,避免了电子阻挡层与电解质层、电子阻挡层与隔层间高温烧结过程中形成高电阻的Ce-Zr固溶体。(2) The present invention adopts magnetron sputtering method to prepare electron blocking layer and interlayer, and the homogeneity of electron blocking layer and interlayer is better, and has avoided the process of high-temperature sintering, has avoided electron blocking layer and electrolyte layer, electron blocking A high-resistance Ce-Zr solid solution is formed during high-temperature sintering between layers and interlayers.
具体实施例specific embodiment
对比例1Comparative example 1
一种固体氧化物电解池,依次包含氢电极层、电解质层和氧电极层。其氢电极为1g,其中NiO和Gd0.2Ce0.8O2分别为0.5g,氢电极层厚度为1000纳米,孔隙率为45%,电解质为Gd0.2Ce0.8O2,电解质层厚度为10微米,氧电极为La0.6Sr0.4Co0.2Fe0.8O3-Gd0.2Ce0.8O2,质量为0.01g,其中La0.6Sr0.4Co0.2Fe0.8O3为0.006g,Gd0.2Ce0.8O2为0.004g,氧电极层厚度为50微米,氧电极层孔隙率为50%。在550℃下,氢电极侧绝对湿度为3%时电解池的OCV为0.97,绝对湿度为50%时电解池OCV为0.8V,1.3V下电流密度为-0.12Acm-2。在450℃下,氢电极侧绝对湿度为3%时电解池的OCV为1.03V,绝对湿度为50%时电解池OCV为0.86V,1.3V下电流密度为-0.03Acm-2。对比例1中电解池包含氢电极层、电解质层和氧电极层,由于电解质层内漏电,电解池的OCV和性能均较低。A solid oxide electrolytic cell sequentially comprises a hydrogen electrode layer, an electrolyte layer and an oxygen electrode layer. The hydrogen electrode is 1g, of which NiO and Gd 0.2 Ce 0.8 O 2 are 0.5g respectively, the thickness of the hydrogen electrode layer is 1000 nm, the porosity is 45%, the electrolyte is Gd 0.2 Ce 0.8 O 2 , and the thickness of the electrolyte layer is 10 microns, The oxygen electrode is La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 -Gd 0.2 Ce 0.8 O 2 , the mass is 0.01g, of which La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 is 0.006g, Gd 0.2 Ce 0.8 O 2 is 0.004g , the thickness of the oxygen electrode layer is 50 microns, and the porosity of the oxygen electrode layer is 50%. At 550°C, the OCV of the electrolytic cell is 0.97 when the absolute humidity of the hydrogen electrode side is 3%, the OCV of the electrolytic cell is 0.8V when the absolute humidity is 50%, and the current density is -0.12Acm -2 at 1.3V. At 450°C, the OCV of the electrolytic cell is 1.03V when the absolute humidity on the side of the hydrogen electrode is 3%, the OCV of the electrolytic cell is 0.86V when the absolute humidity is 50%, and the current density is -0.03Acm -2 at 1.3V. The electrolytic cell in Comparative Example 1 includes a hydrogen electrode layer, an electrolyte layer, and an oxygen electrode layer. Due to leakage in the electrolyte layer, the OCV and performance of the electrolytic cell are low.
实施例1Example 1
一种固体氧化物电解池,依次包括氢电极层、电解质层、电子阻挡层、隔层、氧电极层,其氢电极为1g,其中NiO和Gd0.2Ce0.8O2分别为0.5g,氢电极层厚度为1000纳米,孔隙率为45%,电解质为Gd0.2Ce0.8O2,电解质层厚度为10微米,电子阻挡层材料为Y0.15Zr0.85O2,电子阻挡层厚度为100纳米,隔层材料为Gd0.2Ce0.8O2,隔层厚度为1微米,氧电极为La0.6Sr0.4Co0.2Fe0.8O3-Gd0.2Ce0.8O2,质量为0.01g,其中La0.6Sr0.4Co0.2Fe0.8O3为0.006g,Gd0.2Ce0.8O2为0.004g,氧电极层厚度为50微米,氧电极层孔隙率为50%。在550℃下,氢电极侧绝对湿度为3%时,电解池的OCV为1.02,绝对湿度为50%时电解池OCV为0.86V,1.3V下电流密度为-0.35Acm-2。在450℃下,氢电极侧绝对湿度为3%时,电解池的OCV为1.10,绝对湿度为50%时电解池OCV为0.94V,1.3V下电流密度为-0.15Acm-2。A solid oxide electrolytic cell comprises successively a hydrogen electrode layer, an electrolyte layer, an electron barrier layer, an interlayer, and an oxygen electrode layer, and the hydrogen electrode is 1 g, wherein NiO and Gd 0.2 Ce 0.8 O 2 are 0.5 g respectively, and the hydrogen electrode The thickness of the layer is 1000 nm, the porosity is 45%, the electrolyte is Gd 0.2 Ce 0.8 O 2 , the thickness of the electrolyte layer is 10 microns, the material of the electron blocking layer is Y 0.15 Zr 0.85 O 2 , the thickness of the electron blocking layer is 100 nm, and the interlayer The material is Gd 0.2 Ce 0.8 O 2 , the thickness of the interlayer is 1 micron, the oxygen electrode is La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 -Gd 0.2 Ce 0.8 O 2 , the mass is 0.01g, and La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 is 0.006g, Gd 0.2 Ce 0.8 O 2 is 0.004g, the thickness of the oxygen electrode layer is 50 microns, and the porosity of the oxygen electrode layer is 50%. At 550°C, when the absolute humidity on the side of the hydrogen electrode is 3%, the OCV of the electrolytic cell is 1.02, when the absolute humidity is 50%, the OCV of the electrolytic cell is 0.86V, and the current density at 1.3V is -0.35Acm -2 . At 450°C, when the absolute humidity on the side of the hydrogen electrode is 3%, the OCV of the electrolytic cell is 1.10, when the absolute humidity is 50%, the OCV of the electrolytic cell is 0.94V, and the current density at 1.3V is -0.15Acm -2 .
上述电解池制备过程如下,The above-mentioned electrolytic cell preparation process is as follows,
(1)将NiO(50g)与Gd0.2Ce0.8O2(50g)混合研磨24h后形成氢电极粉体,将氢电极粉体、甲苯、乙醇、鱼油、聚乙二醇、邻苯二甲酸二辛酯和聚乙烯醇缩丁醛混合球磨50h形成氢电极浆料,上述原料用量分别为:100g、80g、25g、1g、3g、3g、8g,将氢电极浆料流延成型后形成氢电极生胚,将生胚干燥后在高温炉中1000℃预烧5h,形成氢电极支撑体;(1) NiO (50g) and Gd 0.2 Ce 0.8 O 2 (50g) were mixed and ground for 24 hours to form a hydrogen electrode powder, and the hydrogen electrode powder, toluene, ethanol, fish oil, polyethylene glycol, phthalic acid di Octyl ester and polyvinyl butyral were mixed and ball-milled for 50 hours to form a hydrogen electrode slurry. The amounts of the above raw materials were: 100g, 80g, 25g, 1g, 3g, 3g, and 8g. The hydrogen electrode slurry was tape-cast to form a hydrogen electrode Embryo, dry the green embryo and pre-fire it in a high-temperature furnace at 1000°C for 5 hours to form a hydrogen electrode support;
(2)将电解质Gd0.2Ce0.8O2粉体与正丁醇、邻苯、聚乙烯醇缩丁醛、鱼油混合研磨10~100h形成电解质浆料,上述原料用量分别为:10g、25g、1.5g、2g、0.2g,采用丝网印刷法将电解质浆料制备到氢电极支撑体上,在高温1400℃烧结10h;(2) Mix and grind the electrolyte Gd 0.2 Ce 0.8 O 2 powder with n-butanol, o-benzene, polyvinyl butyral, and fish oil for 10 to 100 hours to form an electrolyte slurry. g, 2g, 0.2g, the electrolyte slurry was prepared on the hydrogen electrode support by the screen printing method, and sintered at a high temperature of 1400°C for 10h;
(3)采用磁控溅射法制备电子阻挡层,溅射气氛为氧气和氩气混合气,两者流量比为1/15,溅射基底温度为400℃,溅射气压为0.15Pa,溅射功率密度P=10Wcm-2,溅射的电子阻挡层在300℃退火处理;(3) The electron barrier layer was prepared by magnetron sputtering, the sputtering atmosphere was a mixture of oxygen and argon, the flow ratio of the two was 1/15, the sputtering substrate temperature was 400°C, and the sputtering pressure was 0.15Pa. Radiation power density P=10Wcm -2 , the sputtered electron blocking layer is annealed at 300°C;
(4)采用磁控溅射法在电子阻挡层上制备隔层,溅射气氛为氧气和氩气混合气,两者流量比为1/10,溅射基底温度为400℃,溅射气压为0.5Pa,溅射功率密度P=15Wcm-2,溅射后的隔层在1000℃退火处理5h;(4) Prepare an interlayer on the electron blocking layer by magnetron sputtering, the sputtering atmosphere is a mixture of oxygen and argon, the flow ratio of the two is 1/10, the sputtering substrate temperature is 400 °C, and the sputtering pressure is 0.5Pa, sputtering power density P = 15Wcm -2 , the interlayer after sputtering is annealed at 1000°C for 5h;
(5)将La0.6Sr0.4Co0.2Fe0.8O3(6g)、Gd0.2Ce0.8O2(4g)混合研磨10h后与松油醇(4.7g)、乙基纤维素(0.3g)混合再研磨24h形成氧电极浆料,采用丝网印刷法将氧电极浆料制备到隔层上,在高温1000℃烧结3h,得到全电池。(5) La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 (6g), Gd 0.2 Ce 0.8 O 2 (4g) were mixed and ground for 10h, then mixed with terpineol (4.7g), ethyl cellulose (0.3g) and then Grind for 24 hours to form an oxygen electrode slurry, prepare the oxygen electrode slurry on the separator by screen printing, and sinter at a high temperature of 1000°C for 3 hours to obtain a full battery.
实施例2Example 2
一种固体氧化物电解池,依次包括氢电极层、电解质层、电子阻挡层、隔层、氧电极层,其氢电极为1g,其中NiO和Gd0.2Ce0.8O2分别为0.5g,氢电极层厚度为1000纳米,孔隙率为45%,电解质为Gd0.2Ce0.8O2,电解质层厚度为10微米,电子阻挡层材料为Y0.15Zr0.85O2,电子阻挡层厚度为100纳米,隔层材料为Gd0.2Ce0.8O2,隔层厚度为1微米,氧电极为La0.6Sr0.4Co0.2Fe0.8O3-Gd0.2Ce0.8O2,质量为0.01g,其中La0.6Sr0.4Co0.2Fe0.8O3为0.006g,Gd0.2Ce0.8O2为0.004g,氧电极层厚度为50微米,氧电极层孔隙率为50%。A solid oxide electrolytic cell comprises successively a hydrogen electrode layer, an electrolyte layer, an electron barrier layer, an interlayer, and an oxygen electrode layer, and the hydrogen electrode is 1 g, wherein NiO and Gd 0.2 Ce 0.8 O 2 are 0.5 g respectively, and the hydrogen electrode The thickness of the layer is 1000 nm, the porosity is 45%, the electrolyte is Gd 0.2 Ce 0.8 O 2 , the thickness of the electrolyte layer is 10 microns, the material of the electron blocking layer is Y 0.15 Zr 0.85 O 2 , the thickness of the electron blocking layer is 100 nm, and the interlayer The material is Gd 0.2 Ce 0.8 O 2 , the thickness of the interlayer is 1 micron, the oxygen electrode is La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 -Gd 0.2 Ce 0.8 O 2 , the mass is 0.01g, and La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 is 0.006g, Gd 0.2 Ce 0.8 O 2 is 0.004g, the thickness of the oxygen electrode layer is 50 microns, and the porosity of the oxygen electrode layer is 50%.
上述电解池制备过程如下,The above-mentioned electrolytic cell preparation process is as follows,
(1)将NiO(50g)与Gd0.2Ce0.8O2(50g)混合研磨24h后形成氢电极粉体,将氢电极粉体、甲苯、乙醇、鱼油、聚乙二醇、邻苯二甲酸二辛酯和聚乙烯醇缩丁醛混合球磨50h形成氢电极浆料,上述原料用量分别为:100g、80g、25g、1g、3g、3g、8g,将氢电极浆料流延成型后形成氢电极生胚,将生胚干燥后在高温炉中1000℃预烧5h,形成氢电极支撑体;(1) NiO (50g) and Gd 0.2 Ce 0.8 O 2 (50g) were mixed and ground for 24 hours to form a hydrogen electrode powder, and the hydrogen electrode powder, toluene, ethanol, fish oil, polyethylene glycol, phthalic acid di Octyl ester and polyvinyl butyral were mixed and ball-milled for 50 hours to form a hydrogen electrode slurry. The amounts of the above raw materials were: 100g, 80g, 25g, 1g, 3g, 3g, and 8g. The hydrogen electrode slurry was tape-cast to form a hydrogen electrode Embryo, dry the green embryo and pre-fire it in a high-temperature furnace at 1000°C for 5 hours to form a hydrogen electrode support;
(2)将电解质Gd0.2Ce0.8O2粉体与正丁醇、邻苯、聚乙烯醇缩丁醛、鱼油混合研磨10~100h形成电解质浆料,上述原料用量分别为:10g、25g、1.5g、2g∶0.2g,采用丝网印刷法将电解质浆料制备到氢电极支撑体,在高温1400℃烧结10h;(2) Mix and grind the electrolyte Gd 0.2 Ce 0.8 O 2 powder with n-butanol, o-benzene, polyvinyl butyral, and fish oil for 10 to 100 hours to form an electrolyte slurry. g, 2g: 0.2g, prepare the electrolyte slurry to the hydrogen electrode support by the screen printing method, and sinter at a high temperature of 1400°C for 10h;
(3)采用丝网印刷法制备电子阻挡层,将Y0.15Zr0.85O2(10g)与松油醇(10g)、乙基纤维素(0.5g)混合研磨24h得到电子阻挡层浆料,印制到电解质层后,在高温1200℃烧结10h;(3) The electron blocking layer was prepared by screen printing. Y 0.15 Zr 0.85 O 2 (10g) was mixed with terpineol (10g) and ethyl cellulose (0.5g) and ground for 24 hours to obtain the electron blocking layer slurry. After the electrolyte layer is prepared, it is sintered at a high temperature of 1200 ° C for 10 hours;
(4)采用丝网印刷法制备隔层,将Gd0.2Ce0.8O2(8g)与松油醇(10g)、乙基纤维素(0.5g)混合研磨24h得到隔层浆料,印制到电子阻挡后,在高温1280℃烧结10h;(4) The interlayer was prepared by screen printing. Gd 0.2 Ce 0.8 O 2 (8g) was mixed with terpineol (10g) and ethyl cellulose (0.5g) and ground for 24 hours to obtain interlayer slurry, which was printed on After electron blocking, sintering at a high temperature of 1280°C for 10h;
(5)将La0.6Sr0.4Co0.2Fe0.8O3(6g)-Gd0.2Ce0.8O2(4g)混合研磨10h后与松油醇(4.7g)、乙基纤维素(0.3g)混合再研磨24h形成氧电极浆料,采用丝网印刷法将氧电极浆料制备到隔层上,在高温1000℃烧结3h,得到全电池。(5) La 0.6 Sr 0.4 Co 0.2 Fe 0.8 O 3 (6g)-Gd 0.2 Ce 0.8 O 2 (4g) was mixed and ground for 10h, then mixed with terpineol (4.7g) and ethyl cellulose (0.3g) Grind for 24 hours to form an oxygen electrode slurry, prepare the oxygen electrode slurry on the separator by screen printing, and sinter at a high temperature of 1000°C for 3 hours to obtain a full battery.
上述电解池在550℃下,氢电极侧绝对湿度为3%时,电解池的OCV为0.99V,绝对湿度为50%时电解池OCV为0.82V,1.3V下电流密度为-0.15Acm-2。在450℃下,氢电极侧绝对湿度为3%时,电解池的OCV为1.06,绝对湿度为50%时电解池OCV为0.89V,1.3V下电流密度为-0.05Acm-2。The OCV of the above electrolytic cell is 0.99V when the absolute humidity on the side of the hydrogen electrode is 3% at 550°C, the OCV of the electrolytic cell is 0.82V when the absolute humidity is 50%, and the current density at 1.3V is -0.15Acm -2 . At 450°C, when the absolute humidity on the side of the hydrogen electrode is 3%, the OCV of the electrolytic cell is 1.06, when the absolute humidity is 50%, the OCV of the electrolytic cell is 0.89V, and the current density at 1.3V is -0.05Acm -2 .
通过上述例子比较可知,本申请的电解池通过电子阻挡层和隔层的加入,有效的提高了电解池的性能,其中,通过磁控溅射的方式制备电子阻挡层和隔层的电解池性能更优异。By comparing the above examples, it can be seen that the electrolytic cell of the present application effectively improves the performance of the electrolytic cell by adding the electron blocking layer and the interlayer, wherein the electrolytic cell performance of the electron blocking layer and the interlayer is prepared by magnetron sputtering more excellent.
Claims (10)
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