Electrochemical reaction unit and fuel cell stack
US-2016372758-A1 · Dec 22, 2016 · US
US2021043957A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021043957-A1 |
| Application number | US-201916975997-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 22, 2019 |
| Priority date | Feb 27, 2018 |
| Publication date | Feb 11, 2021 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention relates to a proton ceramic fuel cell which has a hydrogen-permeable film as an anode and in which an electrolyte material is BaZrxCe1-x-yYzO3 (x=0.1 to 0.8, z=0.1 to 0.25, x+z≤1.0) (BZCY). An electron-conducting oxide thin film having a film thickness of 1-100 nm is present between a cathode and an electrolyte comprising the material. The present invention also relates to a method for producing a proton ceramic fuel cell having a hydrogen-permeable film as an anode. The method comprises forming a thin film having a thickness of 1-100 nm between a cathode and an electrolyte comprising BZCY, the thin film comprising an electron-conducting oxide. The present invention provides a novel means for improving the output of a PCFC in which BZCY is used in an electrolyte material, and provides a PCFC having an output that exceeds a benchmark of 0.5 W cm−2 at 500° C.
Opening claim text (preview).
1 . A proton ceramics fuel cell in which an electrolyte material is BaZr x Ce 1-x-z Y z O 3 (x=0.1 to 0.8, z=0.1 to 0.25, x+z 23 1.0) and a hydrogen permeable membrane is an anode, wherein the fuel cell comprises an electron conductive oxide thin film having a film thickness in a range of 1 to 100 nm between the electrolyte made of the above material and a cathode. 2 . The fuel cell according to claim 1 , wherein the electron conductive oxide is lanthanum-containing perovskite compound, nickel oxide, manganese oxide, zinc oxide or indium oxide. 3 . The fuel cell according to claim 2 , wherein the lanthanum-containing perovskite compound contains strontium and/or cobalt. 4 . The fuel cell according to claim 2 , wherein the lanthanum-containing perovskite compound is La 0.5 Sr 0.5 CoO 3 . 5 . The fuel cell according to claim 1 , wherein the film thickness of the thin film is in a range of 5 to 80 nm. 6 . The fuel cell according to claim 1 , wherein the electron conductive oxide thin film is an electron conductive oxide agglomerate thin film. 7 . The fuel cell according to claim 1 , wherein operating temperature is in a range of 400 to 600° C. 8 . A method for production of a proton ceramics fuel cell comprising a hydrogen permeable membrane as an anode, wherein the method comprises formation of a thin film having a film thickness in a range of 1 to 100 nm between an electrolyte made of BaZr x Ce 1-x-z Y z O 3 (x=0.1 to 0.8, z=0.1 to 0.25, x+z≤1.0) and a cathode, and the thin film is comprised of an electron conductive oxide. 9 . The method for production according to claim 8 , wherein the electron conductive oxide is lanthanum-containing perovskite compound, nickel oxide, manganese oxide, zinc oxide or indium oxide. 10 . The method for production according to claim 8 , wherein the electron conductive oxide thin film is an electron conductive oxide agglomerate thin film. 11 . The method for production according to claim 8 , wherein the electron conductive oxide thin film is formed by a sputtering method or a sol-gel method. 12 . The fuel cell according to claim 1 , wherein the cathode is a porous cathode. 13 . The fuel cell according to claim 1 , wherein the cathode is a porous cathode and the electron conductive oxide thin film is an electron conductive oxide agglomerate thin film. 14 . The fuel cell according to claim 6 , wherein the electron conductive oxide agglomerate thin film is a polycrystalline thin film, a thin film of an aggregate of amorphous particles or a thin film of a mixture of a polycrystalline and an aggregate of amorphous particles. 15 . The method for production according to claim 8 , wherein the cathode is a porous cathode. 16 . The method for production according to claim 8 , wherein the cathode is a porous cathode and the electron conductive oxide thin film is an electron conductive oxide agglomerate thin film. 17 . The method for production according to claim 10 , wherein the electron conductive oxide agglomerate thin film is a polycrystalline thin film, a thin film of an aggregate of amorphous particles or a thin film of a mixture of a polycrystalline and an aggregate of amorphous particles. 18 . The fuel cell according to claim 1 , wherein the electron conductive oxide is nickel oxide, manganese oxide, zinc oxide or indium oxide. 19 . The method for production according to claim 1 , wherein the electron conductive oxide is nickel oxide, manganese oxide, zinc oxide or indium oxide.
Ion conductive at high temperature · CPC title
the electrolyte consisting of oxides · CPC title
with both reactants being gaseous or vaporised · CPC title
characterised by the electrode/electrolyte combination or the supporting material · CPC title
Non-porous diffusion electrodes, e.g. palladium membranes, ion exchange membranes · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.