CARRIER CARBON MATERIAL FOR SOLID POLYMER FUEL CELL AND CATALYST
    1.
    发明公开
    CARRIER CARBON MATERIAL FOR SOLID POLYMER FUEL CELL AND CATALYST 有权
    用于固体聚合物燃料电池和催化剂的载体炭材料

    公开(公告)号:EP3276717A1

    公开(公告)日:2018-01-31

    申请号:EP16768350.7

    申请日:2016-03-03

    摘要: A support carbon material able to support a catalyst metal in a highly dispersed state and resistant to the flooding phenomenon and with little voltage drop even at the time of large current power generation under high humidity conditions and a catalyst using the same, specifically, a support carbon material for solid polymer type fuel cell use comprised of a porous carbon material which has a pore volume and a pore area found by the BJH analysis method from a nitrogen adsorption isotherm in an adsorption process of a radius 2 nm to 50 nm pore volume V A of 1 ml/g to 5 ml/g and a radius 2 nm to 50 nm pore area S 2-50 of 300 m 2 /g to 1500 m 2 /g and a ratio (V 5-25 /V A ) of radius 5 nm to 25 nm pore volume V 5-25 (ml/g) to said pore volume V A (ml/g) of 0.4 to 0.7 and a ratio (V 2-5 /V A ) of radius 2 nm to 5 nm pore volume V 2-5 (ml/g) to the same of 0.2 to 0.5 and a catalyst using the same.

    摘要翻译: 即使在高湿度条件下的大电流发电时,也能够以高分散状态负载催化剂金属并且耐水淹现象并且电压降低很少的载体碳材料和使用该载体碳材料的催化剂,特别是载体 用于固体高分子型燃料电池用途的碳材料包括多孔碳材料,该多孔碳材料在半径为2nm至50nm的孔隙体积VA的吸附过程中根据氮吸附等温线通过BJH分析方法求得的孔体积和孔面积 为1ml / g至5ml / g,半径为2nm至50nm的孔隙面积S2-50为300m2 / g至1500m2 / g,半径为5nm至25nm的比率(V5-25 / VA) 相对于所述细孔容积VA(ml / g)的细孔容积V5-25(ml / g)为0.4〜0.7,半径为2nm〜5nm细孔容积V2-5的比例(V2-5 / VA) )为0.2〜0.5的催化剂和使用其的催化剂。

    Activated carbon for electricity storage carbon material
    3.
    发明公开
    Activated carbon for electricity storage carbon material 审中-公开
    活性炭用于储电碳材料

    公开(公告)号:EP2722308A1

    公开(公告)日:2014-04-23

    申请号:EP14151451.3

    申请日:2006-12-27

    摘要: The present invention relates to an activated carbon produced by alkali-activating a raw coke or the heat treated product thereof produced by heating a raw coke under atmospheric pressure at a temperature of 550 to 900°C, with an alkali metal hydroxide, wherein the raw coke is produced by coking a feedstock composition at a pressure of 300 to 800 kPa and a temperature of 400 to 600°C. The feedstock composition comprises a first heavy oil with an initial boiling point of 300°C or higher, an asphalten content of 12 percent by mass or less, a saturate content of 60 percent by mass or more and a sulfur content of 0.3 percent by mass or less, produced as a residue resulting from vacuum-distillation of a petroleum-based oil and a second heavy oil with an initial boiling point of 150°C or higher and a sulfur content of 0.5 percent by mass or less, produced as a residue by subjecting a vacuum gas oil or desulfurized vacuum gas oil to fluidized catalytic cracking. The present invention relates also to an electric double layer capacitor comprising said activated carbon.

    摘要翻译: 本发明涉及通过在550〜900℃的温度下在大气压下加热原焦炭而制造的原料焦炭或其热处理物与碱金属氢氧化物进行碱活化而制造的活性炭, 焦炭是通过在300-800kPa的压力和400-600℃的温度下焦化原料组合物而生产的。 原料组合物含有初沸点300℃以上,沥青质含量12质量%以下,饱和含量60质量%以上,硫含量0.3质量%的第一重油 或者更少,作为石油基油和起始沸点为150℃或更高并且硫含量为0.5质量%或更低的第二重油的真空蒸馏得到的残渣产生,作为残余物产生 通过将真空瓦斯油或脱硫真空瓦斯油进行流化催化裂化。 本发明还涉及一种包含所述活性炭的双电层电容器。

    Raw coke for electricity storage carbon material and needle coke
    4.
    发明公开
    Raw coke for electricity storage carbon material and needle coke 审中-公开
    KoksfürelektrizitätsspeicherndesKohlenstoffmaterial undfürNadelkoks

    公开(公告)号:EP2722307A1

    公开(公告)日:2014-04-23

    申请号:EP14151447.1

    申请日:2006-12-27

    摘要: The present invention relates to a raw coke produced by coking a feedstock composition at a pressure of 300 to 800 kPa and a temperature of 400 to 600°C, wherein the feedstock composition comprises a first heavy oil with an initial boiling point of 300°C or higher, an asphalten content of 12 percent by mass or less, a saturate content of 60 percent by mass or more and a sulfur content of 0.3 percent by mass or less, produced as a residue resulting from vacuum-distillation of a petroleum-based oil and a second heavy oil with an initial boiling point of 150°C or higher and a sulfur content of 0.5 percent by mass or less, produced as a residue by subjecting a vacuum gas oil or desulfurized vacuum gas oil to fluidized catalytic cracking, and to a needle coke produced by calcining said raw coke at a temperature of 800 to 1600°C.

    摘要翻译: 本发明涉及通过在300至800kPa的压力和400至600℃的温度下焦化原料组合物而生产的原焦炭,其中原料组合物包含初始沸点为300℃的第一重油 以上,沥青含量为12质量%以下,饱和物含量为60质量%以上,硫含量为0.3质量%以下,作为以石油类为原料的真空蒸馏得到的残渣 油和初始沸点为150℃以上且硫含量为0.5质量%以下的第二重油,通过使真空瓦斯油或脱硫减压瓦斯油进行流化催化裂化而作为残渣而生成,以及 涉及通过在800至1600℃的温度下煅烧所述原焦炭而生产的针状焦炭。

    High capacity hydrogen storage material and method of making the same
    6.
    发明公开
    High capacity hydrogen storage material and method of making the same 审中-公开
    Hochleistungs-Wasserstoffspeichermaterial und Verfahren zu dessen Herstellung

    公开(公告)号:EP2147895A1

    公开(公告)日:2010-01-27

    申请号:EP08167805.4

    申请日:2008-10-29

    IPC分类号: C01B3/00 C01B31/08 C01B31/12

    摘要: The present invention provides a high capacity hydrogen storage material in which a plural mesopore channels and fractal networks of nanopore channels communicating therewith and connecting to the micropores are formed in a microporous material, wherein a plural metal particles are formed on the surface of the mesopore and nanopore channels and of the micropores. In another embodiment, the present invention also provides a method for making the hydrogen storage material through oxidizing the microporous material so as to form a plural mesopore channels and fractal networks of nanopore channels, both of which are connected to the micropores to form a base for the deposition of metal particles capable of decomposing hydrogen molecules into hydrogen atoms. The high capacity hydrogen storage material is capable of increasing the capacity of hydrogen storage, and besides, the oxidizing process for making the hydrogen storage material is simple and has merits of saving cost.

    摘要翻译: 本发明提供了一种高容量储氢材料,其中在微孔材料中形成多孔介孔和与之连通的纳米孔通道分形网络,其中在中孔表面形成多个金属颗粒, 纳米孔通道和微孔。 在另一个实施方案中,本发明还提供一种通过氧化微孔材料制备储氢材料以形成纳米孔通道的多个中孔通道和分形网络的方法,二者均与微孔连接,形成基底 能够将氢分子分解成氢原子的金属颗粒的沉积。 高容量储氢材料能够提高储氢能力,此外,用于制造储氢材料的氧化工艺简单,并且具有节约成本的优点。

    OXIDATION REACTION CATALYST AND PROCESS FOR PRODUCING COMPOUND USING THE SAME
    8.
    发明公开
    OXIDATION REACTION CATALYST AND PROCESS FOR PRODUCING COMPOUND USING THE SAME 审中-公开
    KATALYSATORFÜROXIDATIONSREAKENEN UND VERFAHREN ZUR HERSTELLUNG EINER VERBINDUNG DAMIT

    公开(公告)号:EP1806177A1

    公开(公告)日:2007-07-11

    申请号:EP05781566.4

    申请日:2005-09-05

    摘要: It is a problem to be solved by the present invention to provide an oxidation catalyst which, in oxidation of a compound, can efficiently effect oxidation using oxygen in the air as an oxygen source and can be used repeatedly.
    The above-mentioned problem was solved by an activated carbon in which the BET specific surface area S determined by a nitrogen adsorption method and the amount of surface oxygen which will leave in the form of carbon monoxide O CO (% by weight) satisfy formula (I) 4000 CO . By using this oxidation catalyst, it is possible to oxidize a compound having an oxidizable carbon atom linked directly to an aromatic ring, including a heterocyclic ring, to a corresponding aldehyde or keto compound, or to oxidatively dehydrogenate a hydrogen-containing compound to form an unsaturated bond or a cyclic compound, or to oxidatively and dehydrogenatively form a nitrogen-containing heterocyclic ring from an aryl aldehyde and a compound having a pair of adjacent carbon atoms, one of the carbon atoms having an amino group and the other having an amino, hydroxyl or mercapto group.

    摘要翻译: 本发明要解决的问题是提供一种氧化催化剂,其在化合物的氧化中可以有效地利用空气中的氧作为氧源有效地进行氧化并且可以重复使用。 上述问题是通过氮吸附法测定的BET比表面积S和将以一氧化碳OCO(重量%)的形式留下的表面氧的量满足式((重量%))的活性炭来解决的, I)4000

    ADOSRBENT AND PROCESS FOR PRODUCING ADSORBENT
    9.
    发明公开
    ADOSRBENT AND PROCESS FOR PRODUCING ADSORBENT 审中-公开
    吸附及其制造方法吸附

    公开(公告)号:EP1475146A4

    公开(公告)日:2006-03-01

    申请号:EP03703344

    申请日:2003-02-14

    申请人: ARACO KK

    摘要: A ground kenaf core product obtained in a grinding treatment (10) is dissolved in 70% sulfuric acid in an acid-dissolution treatment 20 to give a saccharide phase (saccharide/sulfuric acid solution). Then this saccharide phase is separated from a lignin phase (lignin sulfate) in a centrifugation treatment (30). The saccharide phase is heated at 90 °C for about 2 hours in the presence of sulfuric acid in an acid-heating treatment (40). Then the saccharide (the residue) is diluted with water and filtered in a water-dilution/filtration treatment (50) until the filtrate becomes neutral. Next, the saccharide is washed with water and dried in a water-washing/drying treatment (60) followed by a baking treatment (70) to thereby give a saccharide carbide serving as an adsorbent A.