A PROCESS FOR METHANATION
    11.
    发明申请

    公开(公告)号:WO2022226063A1

    公开(公告)日:2022-10-27

    申请号:PCT/US2022/025541

    申请日:2022-04-20

    Abstract: A process for methanation comprising a first region for flowing a stream over a solid oxide electrolysis cell. In this first region the stream consists of CO2, H2, and H2O, the stream is converted into a first conversion stream, and the solid oxide electrolysis cell is enhanced with a methanation catalyst. The process also has a removal region connected to the first region wherein the removal region is able to flow the first conversion stream away from the solid oxide electrolysis cell.

    FUEL CELLS WITH A LAYERED ELECTROLYTE
    14.
    发明申请

    公开(公告)号:WO2020092555A1

    公开(公告)日:2020-05-07

    申请号:PCT/US2019/058855

    申请日:2019-10-30

    Abstract: A fuel cell is taught comprising an anode support with an anode functional layer situated on top of and in contact with the anode support. A ScCeSZ electrolyte layer is then disposed on top of and in contact with the anode functional layer. A SDC electrolyte layer is then disposed on top of and in contact with the ScCeSZ electrolyte layer. Finally, a cathode layer is disposed on top of and in contact with the SDC electrolyte layer.

    SOLID OXIDE FUEL CELL STACK DESIGN
    15.
    发明申请

    公开(公告)号:WO2019060410A1

    公开(公告)日:2019-03-28

    申请号:PCT/US2018/051743

    申请日:2018-09-19

    Abstract: A device comprising a first solid oxide fuel cell and a second solid oxide fuel cell. The first solid oxide fuel cell comprises a first anode, a first cathode and a first electrolyte, wherein the first electrolyte is positioned between and connected to the first anode and the first cathode. The second solid oxide fuel cell comprises a second anode, a second cathode and a second electrolyte, wherein the second electrolyte is positioned between and connected to the second anode and the second cathode. In this device the cathode distance between the first cathode and the second cathode is less than the anode distance between the first anode and the second anode.

    ANODE CATALYSTS FOR FUEL CELLS
    17.
    发明申请

    公开(公告)号:WO2022098535A1

    公开(公告)日:2022-05-12

    申请号:PCT/US2021/056561

    申请日:2021-10-26

    Abstract: A fuel cell comprising a Ni-based anode. The fuel cell also comprises a catalyst, wherein the catalyst comprises a mixture of: NiO, YSZ, BaCO3, CuO, ZnO, Fe2O3, and Cr2O3. It is envisioned that the fuel cell is operated at temperatures greater than 600 °C.

    METHOD FOR PRODUCING AN INFILTRATED SOLID OXIDE FUEL CELL LAYER

    公开(公告)号:WO2020123639A1

    公开(公告)日:2020-06-18

    申请号:PCT/US2019/065709

    申请日:2019-12-11

    Abstract: A method of producing an infiltrated solid oxide fuel cell (SOFC) layer. The method begins by infiltrating a solution containing a solute into a SOFC layer to produce a primary SOFC layer. The primary SOFC layer is then dried in a heated environment, wherein the heated environment ranges in temperature from about 25 °C to about 100 °C to produce a dry primary SOFC layer. The dry primary SOFC layer is then cooled at a rate less than about 5 °C/min to room temperature to produce a cooled primary SOFC layer. The cooled primary SOFC layer is then heated to a temperature greater than 500 °C then quenching to a temperature from about 10°C to about 30 °C to produce an infiltrated SOFC layer.

    METHOD FOR PRODUCING AN INFILTRATED SOLID OXIDE FUEL CELL LAYER

    公开(公告)号:WO2020123635A1

    公开(公告)日:2020-06-18

    申请号:PCT/US2019/065705

    申请日:2019-12-11

    Abstract: A method of producing an infiltrated solid oxide fuel cell (SOFC) layer. The method begins by infiltrating a solution containing a solute into a SOFC layer to produce a primary SOFC layer. The primary SOFC layer is then dried in a heated environment, wherein the heated environment ranges in temperature from about 25 °C to about 100 °C to produce a dry primary SOFC layer. The dry primary SOFC layer is then cooled at a rate less than about 5 °C/min to room temperature to produce a cooled primary SOFC layer. The cooled primary SOFC layer is then heated to a temperature greater than 500 °C then quenching to a temperature from about 10 °C to about 30 °C to produce an infiltrated SOFC layer.

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