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    • 8. 发明专利
    • Exhaust gas treatment system and operation method thereof
    • 排气处理系统及其操作方法
    • JP2010201358A
    • 2010-09-16
    • JP2009050375
    • 2009-03-04
    • Ebara Corp株式会社荏原製作所
    • KOMAI TETSUOSHINOHARA TOYOJINOMURA NORIHIKOHASHIMOTO YUTAKAKORIYAMA HIDETO
    • B01D53/70B01D53/34
    • PROBLEM TO BE SOLVED: To fully use the treatment capacity of a treatment agent of an exhaust gas treatment apparatus as much as possible, using a centralized piping connecting structure. SOLUTION: An exhaust gas treatment system includes: a plurality of exhaust gas treatment units 14a-14d including treatment tanks 40; a common inlet duct 30 into which an exhaust gas supplied to the plurality of exhaust gas treatment units flows; an outlet duct 32 for exhausting the gas treated in the exhaust gas treatment units; and a central control section 56 for controlling the operation conditions of the exhaust gas treatment units. The exhaust gas treatment system has: sections 42 installed on the downstream sides of the exhaust gas treatment units, and detecting the exhaust gas treatment capacities of the exhaust gas treatment units; outlet valves 44 installed in treated gas outflow lines 24 extending from the exhaust gas treatment units and connected to the outlet duct 32; and treated gas returning lines 46 diverged on the upstream side of the outlet valves from the treated gas outflow lines, and converged to the common inlet duct. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:尽可能充分利用废气处理装置的处理剂的处理能力,使用集中管道连接结构。 解决方案:废气处理系统包括:多个排气处理单元14a-14d,其包括处理槽40; 供给多个排气处理单元的废气流入的公共入口管道30; 用于排出在废气处理单元中处理的气体的出口管道32; 以及用于控制废气处理单元的操作条件的中央控制部分56。 废气处理系统具有:安装在废气处理单元的下游侧的部分42,并且检测废气处理单元的废气处理能力; 出口阀44安装在从排气处理单元延伸并连接到出口管道32的经处理的气体流出管线24中; 并且经处理的气体返回管线46在出口阀的上游侧从经处理的气体流出管线分流,并且会聚到共同的入口管道。 版权所有(C)2010,JPO&INPIT
    • 9. 发明专利
    • Fluidized bed gasification furnace, and pyrolizing gasification method
    • 流化床气化炉,气化气化方法
    • JP2007024492A
    • 2007-02-01
    • JP2006191942
    • 2006-07-12
    • Ebara Corp株式会社荏原製作所
    • HASHIMOTO YUTAKATOYODA YUKI
    • F23G5/027B09B3/00C10J3/00C10J3/56F23C10/02F23G5/30F23G5/50
    • F27B14/10Y02E50/30
    • PROBLEM TO BE SOLVED: To provide a fluidized bed gasification furnace capable of controlling easily and precisely a circulation amount of a fluidizing medium, and capable of transferring easily and stably a pyrolized residue and heat between a gasification chamber and a combustion chamber.
      SOLUTION: This fluidized bed gasification furnace 1 is provided with the gasification chamber 10 for fluidizing the fluidizing medium in its inside, and the combustion chamber 20 for fluidizing the fluidizing medium in its inside. A raw material is pyrolized thermally in the fluidizing medium, in the gasification chamber 10, to generate pyrolized gas and the pylolized residue. The combustion chamber 20 has a combustion part 22 for combusting the pylolized residue to heat the fluidizing medium, and a sedimentation part 24 for sedimenting the heated fluidizing medium. The fluidized bed gasification furnace 1 is provided with a diffuser 71 for supplying fluidizing gas to an area 22a of the combustion part 22 adjacent to the sedimentation part 24 of the combustion chamber 20 to move the fluidizing medium from the combustion part 22 to the sedimentation part 24, and a circulation controller 82 for regulating a flow rate of the fluidizing gas injected from the first diffuser 71 to control the circulation amount of the fluidizing medium.
      COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种能够容易且准确地控制流化介质的循环量并且能够容易且稳定地转移热解残渣和气化室与燃烧室之间的热量的流化床气化炉。 解决方案:该流化床气化炉1设置有用于使流化介质在其内部流化的气化室10和用于使流化介质在其内部流化的燃烧室20。 将原料在流化介质中在气化室10中进行热处理,以产生热解气体和焦化残渣。 燃烧室20具有燃烧部分22,用于燃烧沸石残渣以加热流化介质;以及沉淀部分24,用于沉积加热的流化介质。 流化床气化炉1设置有用于向邻近燃烧室20的沉降部分24的燃烧部分22的区域22a供应流化气体的扩散器71,以将流化介质从燃烧部分22移动到沉降部分 24,以及循环控制器82,用于调节从第一扩散器71喷射的流化气体的流量,以控制流化介质的循环量。 版权所有(C)2007,JPO&INPIT
    • 10. 发明专利
    • Treatment method for waste gas containing sf6
    • 含SF6的废气处理方法
    • JP2010162475A
    • 2010-07-29
    • JP2009006538
    • 2009-01-15
    • Ebara Corp株式会社荏原製作所
    • MORI YOICHIKOMAI TETSUONOMURA NORIHIKOHASHIMOTO YUTAKAOSATO MASAAKI
    • B01D53/68B01D53/34H01L21/3065
    • Y02C20/30Y02P70/605
    • PROBLEM TO BE SOLVED: To provide waste gas treatment method excellent in durability for efficiently decomposing SF 6 . SOLUTION: The treatment method is for decomposing SF 6 by bringing a fluorine-containing compound treatment agent, which is obtained by molding a mixture of Al(OH) 3 and Ca(OH) 2 with an average particle diameter (median diameter) of at least 55 μm and at most 160 μm in a mole ratio of (3:7) to (5:5), drying the molded mixture, and firing the dried mixture in a temperature range higher than 430°C and 890°C or lower in a nitrogen current or air current, and a waste gas containing SF 6 into contact with each other in a temperature range of 550 to 650°C, and when the SF 6 removal efficiency is lowered to 95% or lower during the operation, the fluorine-containing compound treatment agent is replaced. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供耐久性优异的废气处理方法以有效分解SF 6 。 解决方案:通过使含氟化合物处理剂(其通过模制Al(OH)3 SB 3)的混合物而获得,该处理方法用于分解SF 6 和(3:7)至(5:5)的摩尔比的平均粒径(中值粒径)为至少55μm且至多160μm的Ca(OH) 在氮气流或空气流中在高于430℃和890℃或更低的温度范围内焙烧干燥的混合物,以及含有SF 6 的废气与每个 另一方面在550〜650℃的温度范围内,并且当操作中SF 6 去除效率降低至95%以下时,更换含氟化合物处理剂。 版权所有(C)2010,JPO&INPIT