153.
    发明专利
    未知

    公开(公告)号:ES2143861T3

    公开(公告)日:2000-05-16

    申请号:ES97919767

    申请日:1997-05-01

    Abstract: PCT No. PCT/NL97/00247 Sec. 371 Date Nov. 5, 1998 Sec. 102(e) Date Nov. 5, 1998 PCT Filed May 1, 1997 PCT Pub. No. WO97/42674 PCT Pub. Date Nov. 13, 1997Method for determining the utilization of a reactant at the anode side or cathode side of a fuel cell. To this end a low flow with high utilization is applied at the side to be measured and an appreciable flow with low utilization is applied at the other side. A table is compiled in which the relationship between the Nernst voltage under the outlet conditions, such as the temperature, and the utilization of the reactant to be measured is incorporated. Cell voltage is then measured at the outlet and is equated to the Nernst voltage. The utilization can be determined from the table. This method can be used for determination of the flow rate and the flow distribution in a stack of electrochemical cells.

    Fuel cell and fuel cell stack provided with a matrix plate seal

    公开(公告)号:AU3736799A

    公开(公告)日:1999-11-23

    申请号:AU3736799

    申请日:1999-05-04

    Abstract: Fuel cell and fuel cell stack, more particularly an MCFC cell. A matrix plate (7) is placed between anode (3) and cathode (2). At the location of the gas supply/discharge means (18) a seal between said gas supply and discharge means and with respect to the surroundings is provided by a matrix plate. The latter consists of a metallic component that is provided with small elevations (27) which press on the matrix. It has been found that cracking and gas leakage can be prevented by this means.

    ELECTROCHEMICAL CELL WITH SINTERED ANODE OF METALLIC PARTICLES AND OXIDES

    公开(公告)号:CA2330661A1

    公开(公告)日:1999-11-11

    申请号:CA2330661

    申请日:1999-05-04

    Abstract: Anode (1) for an electrochemical cell and method for the production thereof. This anode consists of a mixture of electron- and ion-conducting particles. The ion-conducting particles consist of oxides. The anode is made up in such a way that that part (3) of anode located close to the electrolyte (2) compris es small oxygen-ion-conducting particles, whilst the part (4) located closer to the current collector comprises coarser oxide particles. By this means it is possible to provide for optimum adaptation to the various requirements which are imposed in respect of the behaviour of the anode located at the electrolyte or at the current collector (6).

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