HYDROGEN REFORMING METHOD AND HYDROGEN REFORMING DEVICE USING OXYGEN-PERMEABLE MEMBRANE
    2.
    发明公开
    HYDROGEN REFORMING METHOD AND HYDROGEN REFORMING DEVICE USING OXYGEN-PERMEABLE MEMBRANE 有权
    重整制氢工艺及重整制氢装置中使用透氧膜

    公开(公告)号:EP2045212A1

    公开(公告)日:2009-04-08

    申请号:EP06811803.3

    申请日:2006-10-16

    摘要: [Objects] To provide a method and an apparatus for reforming a hydrocarbon with a prolonged life of an oxygen-permeable membrane and a high recovery rate.
    [Solutions] The oxygen-permeable membrane absorbs the free energy change, ΔG, of a partial oxidation reforming reaction and then converts it into work for oxygen isolation and Joule heat, Q. Here, as seen in Table 1 and Fig. 1 , ΔG of the partial oxidation reforming reaction is approximately ten times larger than ΔH, and further increases as the temperature increases. The generated Joule heat, Q, has to be removed at a high efficiency, and this removal process is achieved by returning a portion of the Joule heat to the system as the entropy change, TΔS, of the partial oxidation reaction itself and by steam reforming using the total energy change, ΔH.

    摘要翻译: [对象为了用于与氧渗透膜的延长的寿命和高的回收率重整的烃的速率提供的方法和装置。 [解决方案]氧渗透膜吸收自由能变化,“G,部分氧化重整反应,然后将其转换成工作氧气隔离和焦耳热,Q.这里,如在表1和图1所示, “部分氧化重整反应的G是大于约10倍” H,并且进一步增加随着温度的升高。 所产生的焦耳热,Q,具有以高效率进行去除,该去除处理是通过向系统为熵变,T“S,部分氧化反应本身以及通过焦耳热的一部分返回取得 蒸汽重整使用的总能量的变化,“H。

    ELECTROCHEMICAL CELL AND METHOD FOR PRODUCING ELECTROCHEMICAL CELL
    4.
    发明公开
    ELECTROCHEMICAL CELL AND METHOD FOR PRODUCING ELECTROCHEMICAL CELL 有权
    电化学电池及其制造方法电化学电池

    公开(公告)号:EP1953540A1

    公开(公告)日:2008-08-06

    申请号:EP06833002.6

    申请日:2006-11-21

    摘要: [Object] An electrochemical cell including a proton conductor as an electrolyte with superior stability, particularly against gases containing carbon dioxide, is provided.
    [Solving Means] A proton-conductive electrolyte 21 used for an electrochemical cell 20B was a ceramic having the composition SrZr 0.5 Ce 0.4 Y 0.1 O 3-δ . As the cathode, a thin film of a proton conductor having the composition SrCe 0.95 Yb 0.05 O 3-δ was provided on the electrolyte 21 as an intermediate layer 22, and a porous platinum electrode 23c was provided thereon. The anode used was a palladium electrode 23a. A cell 20A including no intermediate layer 22 had a high overvoltage approaching 600 mV at a low current density, namely, 70 mA/cm 2 . In contrast, the cell 20B, including the intermediate layer 21, had a low overvoltage, namely, about 170 mV, at a current density of 680 mA/cm 2 .

    摘要翻译: [对象]一种电化学电池,包括质子导体为具优良稳定性电解质,特别是针对气含有二氧化碳,提供。 [解决手段]一种质子传导性电解质用于在电化学电池20B其中的陶瓷具有组成SrZr 0.5的Ce 0.4 y在0.1 O 3” 21。 作为阴极,质子导体的薄膜具有作为中间层22被设置在电解质21的组合物SRCE 0.95镱0.05 O 3”,并且其设置在其上的多孔铂电极23c中。 所用的阳极是钯电极23a。 甲单元20A不包括中间层22具有高的过电压接近600毫伏在低电流密度,即,70%毫安/厘米2。 相反,单元20B包含在中间层21具有低的过压,即,约170毫伏,在680毫安/厘米2的电流密度。