Fabrication of Fuel Cells with Ceramic Gas Separation Membrane

陶瓷气体分离膜燃料电池的制造

基本信息

  • 批准号:
    06650952
  • 负责人:
  • 金额:
    $ 1.28万
  • 依托单位:
  • 依托单位国家:
    日本
  • 项目类别:
    Grant-in-Aid for General Scientific Research (C)
  • 财政年份:
    1994
  • 资助国家:
    日本
  • 起止时间:
    1994 至 1995
  • 项目状态:
    已结题

项目摘要

Ceramic gas separation membrane has been regarded to be thermally stable and resistant to various atmospheres. The present investigation aims at the application of the ceramic separation membrane to the phosphoric acid fuel cell without gas sealing. One of two electrode for the phosphoric acid fuel cell is covered with the membrane with hydrogen selective permeation, whereas the other electrode is open to the atmosphere. This structure may enables to produce voltage from the gaseous mixture of fuel and oxidant. The change of the atmosphere from H_2 to N_2 resulted in transient positive voltage for phosphoric acid fuel cell with Al_2O_3 membrane. On the contrary the switch of gaseous atmosphere from N_2 to H_2 produces negative voltage, whereas the terminal voltage rapidly approaches to zero. A current could be also derived from the above-mentioned fuel cell without gas sealing. However, it was not possible to obtain output voltage continuously because of the insufficient permeation selectivity. The Al_2O_3 plate, Al_2O_3 membrane, and Rh-Al_2O_3 membrane were respectively used for the membrane reactor for methanol steam reforming reaction (CH_3OH+H_2O*3H_2+CO_2). The conversion rose up quite steeply in every case with increasing temperature to 250゚C.Complete conversion of methanol was attained in the case of the membrane reactors. Following sequence was obtained for the conversion of methanol ; Fixed bed reactor <reactor with porous Al_2O_3 plate <Al_2O_3 membrane rector <Rh-Al_2O_3 membrane reactor. The produced hydrogen could be effectively removed from the reaction system by the membrane. This situation gave rise to the high overall conversion, especially by use of Rh-Al_2O_3 membrane. High H_2/CO_2 ratio was attained for the gas in the permeation side.
陶瓷气体分离膜被认为是热稳定的,并且耐受各种气氛。本研究旨在将陶瓷分离膜应用于无气封磷酸燃料电池。磷酸燃料电池的两个电极之一覆盖有具有氢选择性渗透的膜,而另一个电极向大气开放。该结构可以使得能够从燃料和氧化剂的气体混合物产生电压。当气氛由H_2转变为N_2时,Al_2O_3膜磷酸燃料电池产生了瞬态正电压。相反,当气氛由N_2切换到H_2时,端电压迅速趋于零,而当气氛由N_2切换到H_2时,端电压迅速趋于零。也可以从上述没有气体密封的燃料电池获得电流。然而,由于渗透选择性不足,不可能连续获得输出电压。将Al_2O_3平板、Al_2O_3膜和Rh-Al_2 O_3膜分别用于甲醇水蒸气重整反应(CH_3OH+H_2O*3H_2+CO_2)的膜反应器。在每种情况下,随着温度升高到250 ℃,转化率都急剧上升。在膜反应器的情况下,甲醇完全转化。甲醇转化率的顺序为:固定床反应器<多孔Al_2O_3板反应器<Al_2O_3膜反应器<Rh-Al_2 O_3膜反应器。该膜可有效地将生成的氢气从反应体系中去除。这种情况导致了高的总转化率,特别是使用Rh-Al_2 O_3膜。渗透侧气体的H_2/CO_2比较高。

项目成果

期刊论文数量(20)
专著数量(0)
科研奖励数量(0)
会议论文数量(0)
专利数量(0)
K.Eguchi,M.Chai,M.Machida,H.Arai: "Metal Dispersed Porous Alumina Membrane for Selective Hydrogen Permeation and its application to Membrane Reactor for Methane Steam Reforming" Proceedings of TOCAT2. (印刷中). (1995)
K. Eguchi、M. Chai、M. Machida、H. Arai:“用于选择性氢渗透的金属分散多孔氧化铝膜及其在甲烷蒸汽重整膜反应器中的应用”TOCAT2 论文集(1995 年)。
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    0
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K. Eguchi, Y. Kunisa, K. Adachi, M. Kayano, K. Sekizawa, H. Arai: "An Effect of Anodic Reaction on the Current-Voltage Characteristics of Solid Oxide Fuel Cells" Chemistry Letters. 963-964 (1995)
K. Eguchi、Y. Kunisa、K. Adachi、M. Kayano、K. Sekizawa、H. Arai:“阳极反应对固体氧化物燃料电池电流电压特性的影响”化学快报。
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K.Eguchi, M.-R.Chai, M.Machida, H.Arai: "Matal Dispersed Porous Alumina Membrane for Selective Hydrogen Permeation and its Application to Membrane Reactor for Methane Steam Reforming" Science and Technology in Catalysis. 251-256 (1995)
K.Eguchi、M.-R.Chai、M.Machida、H.Arai:“用于选择性氢渗透的金属分散多孔氧化铝膜及其在甲烷蒸汽重整膜反应器中的应用”催化科学与技术。
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    0
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K.Eguchi, Y.Kunisa, K.Adachi, M.Kayano, K.Sekizawa, H.Arai: ""An Effect of Anodic Reaction on the Current-Voltage Characteristics of Solid Oxide Fuel Cells"" Chemistry Letters. 963-964 (1995)
K.Eguchi、Y.Kunisa、K.Adachi、M.Kayano、K.Sekizawa、H.Arai:“阳极反应对固体氧化物燃料电池电流电压特性的影响”化学快报。
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    0
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K.Eguchi, Y.Kunisa, K.Adachi, M.Kayano, K.Sekizawa, H.Arai: "An Effect of Anodic Reaction on the Current-Voltage Characteristics of Solid Oxide Fuel Cells" Chemistry Letters. 963-964 (1995)
K.Eguchi、Y.Kunisa、K.Adachi、M.Kayano、K.Sekizawa、H.Arai:“阳极反应对固体氧化物燃料电池电流电压特性的影响”化学快报。
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EGUCHI Koichi其他文献

EGUCHI Koichi的其他文献

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{{ truncateString('EGUCHI Koichi', 18)}}的其他基金

Hydrogen production and separation processes employing proton conductor and water-gas shift reaction catalyst
采用质子导体和水煤气变换反应催化剂的氢气生产和分离方法
  • 批准号:
    19360366
  • 财政年份:
    2007
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
Basic Sorption-Desorption Characteristics of NOx and SOx by Mixed Oxide Sorbents
混合氧化物吸附剂对 NOx 和 SOx 的基本吸附-解吸特性
  • 批准号:
    16360402
  • 财政年份:
    2004
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
Fuel Reforming and CO Removal for Transportable Hydrogen Production Systems
可运输制氢系统的燃料重整和二氧化碳去除
  • 批准号:
    11450308
  • 财政年份:
    1999
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B)
Development of new sorbent material for reversible removal of air pollutants using catalytic reactions
开发利用催化反应可逆去除空气污染物的新型吸附剂材料
  • 批准号:
    10555280
  • 财政年份:
    1998
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (B).
Investigation of efficient electro chemical reactor utilizing hydrogen
利用氢气的高效电化学反应器的研究
  • 批准号:
    09650908
  • 财政年份:
    1997
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (C)
Development of Metal Oxide Materials for Rapid and Reversible DeNOx by Absorption into Solid Phase
固相吸收快速可逆脱硝金属氧化物材料的开发
  • 批准号:
    07555198
  • 财政年份:
    1995
  • 资助金额:
    $ 1.28万
  • 项目类别:
    Grant-in-Aid for Scientific Research (A)

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