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    • 82. 发明专利
    • Transport method of fluid catalytic cracking catalyst
    • 流体催化裂化催化剂运输方法
    • JP2009132836A
    • 2009-06-18
    • JP2007311388
    • 2007-11-30
    • Nippon Oil CorpPetroleum Energy Center新日本石油株式会社財団法人石油産業活性化センター
    • SAKOTA HISAO
    • C10G11/18
    • C10G11/18
    • PROBLEM TO BE SOLVED: To provide a transport method of a fluid catalytic cracking catalyst by which the friction in a curved part of a transport pipe line for the transport of the fluid catalytic cracking catalyst (FCC catalyst) in a dry state is remarkably reduced.
      SOLUTION: The transport method of the FCC catalyst is provided with a transport step of transporting the FCC catalyst using a gas by causing the gas to flow in the transport pipe line having the curved part. The transport pipe is made of a metallic material and the curved part is constituted of a linear first part and a linear second part connected to the first part. In the transport step, the space velocity of the gas is controlled to ≥5 m/s and ≤20 m/s, the angle of the flow direction of the gas flowing in the second part to the flow direction of the gas flowing in the first part is controlled to ≥45° and ≤90° and the concentration of the FCC catalyst is controlled to ≥5 g/L and ≤10 g/L or ≥15 g/L and ≤20 g/L.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种流化催化裂化催化剂的输送方法,其中用于输送干燥状态的流化催化裂化催化剂(FCC催化剂)的运输管线的弯曲部分的摩擦是 明显减少 解决方案:FCC催化剂的输送方法具有通过使气体在具有弯曲部分的输送管线中流动而使用气体输送FCC催化剂的输送步骤。 输送管由金属材料制成,弯曲部分由直线的第一部分和连接到第一部分的直线的第二部分构成。 在输送步骤中,将气体的空间速度控制在≥5m/ s和≤20m/ s,在第二部分中流动的气体的流动方向与在 第一部分控制在≥45°和≤90°,FCC催化剂的浓度控制在≥5g / L,≤10g / L或≥15g / L和≤20g / L。 版权所有(C)2009,JPO&INPIT
    • 86. 发明专利
    • Method for producing gasoline base material and gasoline
    • 汽油基材料和汽油的生产方法
    • JP2009096830A
    • 2009-05-07
    • JP2007267031
    • 2007-10-12
    • Nippon Oil Corp新日本石油株式会社
    • HATANAKA SHIGETOSHIMADA KOJIIKI SUGURU
    • C10G65/02C10G45/06C10G45/08C10L1/06
    • C10G11/00C10G45/02C10G45/04C10G65/04C10G69/04C10G2300/104C10G2300/1044C10G2300/202C10G2300/301C10G2300/4018C10G2400/02C10L1/06
    • PROBLEM TO BE SOLVED: To provide a method for producing a gasoline base material which has a sulfur content of ≤10 ppm by mass and can be used as a base material for sulfur-free gasoline by subjecting catalytically cracked gasoline to hydrodesulfurization while suppressing the reduction in the octane value to the extent causing no trouble in practical use; and to provide gasoline containing the gasoline base material obtained by the same.
      SOLUTION: The method for producing the gasoline base material includes: a first process for subjecting catalytically cracked gasoline to hydrodesulfurization so that the hydrogenation ratio of olefins contained in the catalytically cracked gasoline becomes ≤25 mol%, the content of total sulfur becomes ≤20 ppm by mass, the content of sulfur originating in thiophenes and benzothiophenes becomes ≤5 ppm by mass, and the content of sulfur originating in thiacyclopentanes becomes ≤0.1 ppm by mass, based on the mass of product oil; and a second process for further subjecting the product oil in the first process to hydrodesulfurization so that the total of the hydrogenation ratios of olefins in the first process and this process becomes ≤30 mol%, the content of total sulfur becomes ≤10 ppm by mass, and the content of sulfur originating in thiols becomes ≤5 ppm by mass, based on the mass of product oil.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 解决问题的方法:提供一种硫含量≤10质量ppm的汽油基材的制造方法,可以通过使催化裂化汽油进行加氢脱硫而用作无硫汽油的基材,同时 抑制辛烷值降低至实际使用不麻烦的程度; 并提供含有由其获得的汽油基料的汽油。 解决方案:汽油基材的制造方法包括:使催化裂化汽油进行加氢脱硫,使催化裂化汽油中所含的烯烃的氢化比例为≤25摩尔%的第一种方法,总硫含量变为 ≤20质量ppm时,源于噻吩和苯并噻吩的硫含量为≤5质量ppm,根据产品油的质量,来自硫氢环戊烷的硫含量为≤0.1质量ppm; 以及第二种方法,用于在第一种方法中对产物油进行加氢脱硫,使得第一种方法和该方法中的烯烃的氢化比例总计为≤30mol%,总硫含量变成≤10质量% ,硫醇的硫含量相对于产品油的质量为≤5质量ppm。 版权所有(C)2009,JPO&INPIT
    • 87. 发明专利
    • Reforming apparatus for fuel cell
    • 燃料电池改造装置
    • JP2009096706A
    • 2009-05-07
    • JP2008070055
    • 2008-03-18
    • Nippon Oil CorpSanyo Electric Co Ltd三洋電機株式会社新日本石油株式会社
    • FUJIO AKIRAKADOWAKI MASATAKASATO YASUSHISAMURA TAKESHI
    • C01B3/38C01B3/48H01M8/06
    • Y02E60/50
    • PROBLEM TO BE SOLVED: To provide a reforming apparatus for a fuel cell with a simple constitution. SOLUTION: In a reforming apparatus, for use in a fuel cell, for reforming a raw fuel into a hydrogen-rich reformed gas, a reformer 12 generates the reformed gas from the raw fuel. A shift reactor 14 reduces carbon monoxide contained in the reformed gas through a shift reaction. A selective oxidation unit 16 reduces the carbon monoxide contained in the reformed gas that has passed through the shift reactor 14 by performing selective oxidation on the carbon monoxide. A reforming reaction tube 18 houses linearly the reformer 12, the shift reactor 14 and the selective oxidation unit 16 in this order, and further houses a desulfurization unit 160. A combustion means produces combustion exhaust gas by combusting the raw fuel. An outer casing 22 is placed around the reforming reaction tube 18, and the outer casing 22 has a large diameter than that of the reforming reaction tube 18. A heated flow passage 32 through which the combustion exhaust gas passed to heat the reforming reaction tube 18 is formed between the reforming reaction tube 18 and the outer casing 22. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种具有简单结构的燃料电池重整装置。 解决方案:在用于燃料电池的重整装置中,用于将原料燃料重整成富氢重整气体,重整器12从原燃料产生重整气体。 换档反应器14通过换档反应来还原重整气中所含的一氧化碳。 选择性氧化单元16通过对一氧化碳进行选择性氧化来减少已经通过变换反应器14的重整气体中所含的一氧化碳。 重整反应管18按顺序容纳重整器12,换档反应器14和选择氧化单元16,并且还容纳脱硫单元160.燃烧装置通过燃烧原燃料来产生燃烧废气。 外壳22设置在重整反应管18周围,外壳22的直径大于重整反应管18的直径。加热流路32,通过燃烧废气加热重整反应管18 形成在重整反应管18和外壳22之间。版权所有(C)2009,JPO&INPIT