Method for manufacturing tubular co-electrolysis cell

US2017275769A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2017275769-A1
Application numberUS-201515129660-A
CountryUS
Kind codeA1
Filing dateApr 30, 2015
Priority dateDec 18, 2014
Publication dateSep 28, 2017
Grant date

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The present invention relates to a method for manufacturing a tubular co-electrolysis cell which is capable of producing synthesis gas from water and carbon dioxide, and a tubular co-electrolysis cell prepared by the preparing method. The present invention comprises a tubular co-electrolysis cell which comprises: a cylindrical support comprising NIO and YSZ: a cathode layer formed on a surface of the cylindrical support, the cathode layer comprising (Sr 1-x La x )Ti 1-y M y )O 3 (M=V, Nb, Co, Mn); a solid electrolyte layer formed on the surface of the cathode layer; and an anode layer formed on a surface of the solid electrolyte layer. The tubular co-electrolysis cell manufactured by the method for manufacturing the tubular co-electrolysis cell of the present in has an excellent synthesis gas conversion rate and is capable of producing synthesis gas even at a low over voltage.

First claim

Opening claim text (preview).

1 . A tubular co-electrolysis cell, comprising: a cylindrical support including NIO and YSZ; a cathode layer comprising (Sr 1-x La x )(Ti 1-y M y )O 3 (M=V, Nb, Co, Mn) formed on a surface of the cylindrical support; a solid electrolyte layer formed on a surface of the cathode layer; and an anode layer formed on a surface of the solid electrolyte layer. 2 . The tubular co-electrolysis cell of claim 1 , wherein the solid electrolyte layer comprises one or more selected from the group consisting of YSZ (yttria stabilized zirconia) LSGM (strontium (Sr)- and magnesium (Mg)-doped lanthanium gallate), ScSZ (scandia stabilized zirconium oxide) GDC (gadlinium-doped ceria), and SDC (samaria-doped ceria). 3 . The tubular co-electrolysis cell of claim 1 , wherein the anode layer comprises a LSCF-GDC or YSZ-LSM and LSM complex. 4 . The tubular co-electrolysis cell of claim 1 , wherein the anode layer comprises a LSCF-GDC or YSZ-LSM and LSM complex. 5 . A method for preparing a tubular co-electrolysis cell, the method comprising: a step 1 of mixing NIO, YSZ, and a pore forming agent, mixing with a solvent into a type of slurry, and ball-milling the slurry; a step 2 of drying and then powdering the slurry; a step 3 of producing a support for the co-electrolysis cell by adding an additive to the powdered mixture and kneading to produce a paste, and extruding the paste; a step 4 of rolling-drying the extruded support for the co-electrolysis cell; and a step 5 of pre-sintering the rolling-dried support for the co-electrolysis cell and then coating the support with a cathode, an electrolyte, and an anode, wherein the cathode comprises a (Sr 1-x La x )(Ti 1-y , M y )O 3 (M=V, Nb, Co, Mn). 6 . The method of claim 5 , wherein the pore forming agent comprises one or more selected from the group consisting of active carbon and carbon black. 7 . The method of claim 5 , wherein the additive comprises a binder, a plasticizer, and a lubricant. 8 . The method of claim 5 , wherein the pre-sintering is performed by stepwise-heating including heating up to 300° C. to 400° C., then to 700° C. to 800° C. and then 1000° C. to 1200° C. 9 . The method of claim 5 , wherein the cathode and the anode are coated by dip coating. 10 . The method of claim 9 , wherein the cathode is coated and is then thermally treated at 800° C. to 1200° C. 11 . The method of claim 9 , wherein the anode is coated and is then thermally treated at 900° C. to 1400° C. 12 . The method of claim 5 , wherein the electrolyte is coated by vacuum slurry coating. 13 . The method of claim 12 , wherein the electrolyte is coated and is then thermally treated at 1200° C. to 1600° C. 14 . The method of claim 5 , wherein a fuel used in the cathode comprises H 2 O, CO 2 and H 2 . 15 . A tubular co-electrolysis cell prepared by the method of claim 5 . 16 . (canceled)

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Inventors

Classifications

  • Chemistry & Metallurgy · mapped topic

  • C25B1/02Primary

    Hydrogen or oxygen · CPC title

  • Details (electrodes H01M4/86 - H01M4/98) · CPC title

  • Fuel cells with solid electrolytes · CPC title

  • operating at high temperature, e.g. with stabilised ZrO2 electrolyte · CPC title

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What does patent US2017275769A1 cover?
The present invention relates to a method for manufacturing a tubular co-electrolysis cell which is capable of producing synthesis gas from water and carbon dioxide, and a tubular co-electrolysis cell prepared by the preparing method. The present invention comprises a tubular co-electrolysis cell which comprises: a cylindrical support comprising NIO and YSZ: a cathode layer formed on a surface …
Who is the assignee on this patent?
Korea Energy Research Inst
What technology area does this patent fall under?
Primary CPC classification C25B1/02. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Sep 28 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).