首页> 外国专利> SUPPORT FOR POLYMER ELECTROLYTE FUEL CELL CATALYST, METHOD OF PRODUCING SUPPORT FOR POLYMER ELECTROLYTE FUEL CELL CATALYST, CATALYST LAYER FOR POLYMER ELECTROLYTE FUEL CELL, AND FUEL CELL

SUPPORT FOR POLYMER ELECTROLYTE FUEL CELL CATALYST, METHOD OF PRODUCING SUPPORT FOR POLYMER ELECTROLYTE FUEL CELL CATALYST, CATALYST LAYER FOR POLYMER ELECTROLYTE FUEL CELL, AND FUEL CELL

机译:高分子电解质燃料电池用催化剂的支持,高分子电解质燃料电池用催化剂的制造方法,高分子电解质燃料电池的催化剂层和燃料电池

摘要

A solid polymer-type fuel cell catalyst carrier which satisfies the following requirements (A), (B), (C), and (D), a method for manufacturing the same, a catalyst layer for a solid polymer-type fuel cell, and a fuel cell. (A) The specific surface area according to a BET analysis of a nitrogen adsorption isotherm is 450 to 1500 m2/g. (B) A nitrogen adsorption-desorption isotherm forms a hysteresis loop in a range of relative pressure P/P0 = more than 0.47 to 0.90, where the area ?S0.47-0.9 of the hysteresis loop is 1 to 35 mL/g. (C) The relative pressure Pclose/P0 at which the hysteresis loop is closed is more than 0.47 to 0.70. (D) The half-value width of G-band detected in a range of 1500 to 1700 cm-1 according to Raman spectrometry is 45 to 75 cm-1.
机译:满足以下要求(A),(B),(C)和(D)的固体聚合物型燃料电池催化剂载体,其制造方法,用于固体聚合物型燃料电池的催化剂层,和燃料电池。 (A)根据氮吸附等温线的BET分析,比表面积为450至1500m2 / g。 (B)氮吸附-解吸等温线在相对压力P / P0 =大于0.47至0.90的范围内形成磁滞回线,其中磁滞回线的面积ΔS0.47-0.9为1至35mL / g。 (C)使磁滞回路闭合的相对压力Pclose / P0大于0.47至0.70。 (D)根据拉曼光谱法在1500至1700cm-1的范围内检测到的G带的半值宽度为45至75cm-1。

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