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    • 1. 发明专利
    • Gasification reactor for forming combustible gas
    • 用于形成可燃气体的气化反应器
    • JP2009067979A
    • 2009-04-02
    • JP2008042774
    • 2008-02-25
    • National Institute Of Advanced Industrial & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHIKURAMOTO KOJISUZUKI ZENZO
    • C10J3/46C10B49/06C10J3/00C10J3/02
    • PROBLEM TO BE SOLVED: To provide a gasification reactor for obtaining a combustible gas utilizing organic resources (biomass, refuse, sewage sludge, etc.), coal, etc. as a hydrocarbon-based solid fuel, wherein, an amount of a combustible gas obtainable from a combustion furnace is increased by accelerating gasification of high char-content fuel at low temperature, thus the combustible gas is obtained in a high efficiency.
      SOLUTION: The reactor for gasifying hydrocarbon-based solid fuels is equipped with, each independently, an alkali-adsorbing furnace, wherein adsorption of alkali and/or alkali earth metals evaporated in a course of thermal cracking of hydrocarbon-based solid fuels such as organic resources, coal, etc. are performed actively, a gasification furnace for gasifying char introduced from the alkali-adsorbing furnace, and a combustion furnace for forming a combustion gas by burning a residual char introduced from the gasification furnace, wherein, absorption efficiency of alkali and/or alkali earth metals by char is made higher by making the alkali-adsorbing furnace a moving bed-type.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种利用有机资源(生物质,垃圾,污水污泥等),煤等作为烃类固体燃料获得可燃气体的气化反应器,其中, 通过在低温下加速高焦炭燃料的气化,可以提高从燃烧炉获得的可燃气体,从而高效率地获得可燃性气体。 解决方案:用于气化烃类固体燃料的反应器各自独立地装备有碱吸附炉,其中碱金属和/或碱土金属的吸附在烃类固体燃料的热裂解过程中蒸发 主动进行有机资源,煤等的制造,从碱吸附炉引入的气化气化炉,燃烧从气化炉引入的残留焦炭形成燃烧气体的燃烧炉,其中吸收 通过使碱吸附炉成为移动床型,通过焦炭使碱金属和/或碱土金属的效率提高。 版权所有(C)2009,JPO&INPIT
    • 3. 发明专利
    • Gasification system recycling active charcoal drawn out from tar absorption tower
    • 气化系统回收活性炭从塔吸收塔抽出
    • JP2009046644A
    • 2009-03-05
    • JP2007216820
    • 2007-08-23
    • National Institute Of Advanced Industrial & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHIKURAMOTO KOJISUZUKI ZENZO
    • C10J3/00B09B3/00C02F11/10
    • Y02E50/30
    • PROBLEM TO BE SOLVED: To provide a gasification system, which uses a gasification furnace for utilizing organic resources of biomass, refuse, sewer sludge, etc. and coal or the like as hydrocarbon-based solid fuels, as can make effective use of an active charcoal drawn out of a tar absorptioon tower provided in the downstream and as can achieve a comprehensive gasification efficiency by promoting the gasification of char inside the gasification furnace. SOLUTION: The gasification system, which uses a gasification reaction furnace for hydrocarbon-based solid fuels and is provided with an alkali absorption furnace for adsorbing the alkali evaporating at the time of the thermal decomposition of the hydrocarbon-based solid fuels onto char, with a gasification furnace for gasifying the char introduced from the above alkali absorption furnace, and with a combustion furnace for generating a combustive gas by burning the residual char introduced from the above gasification furnace, each of these being connected in this order through the communicating passages, is characterized in that the active charcoal drawn out of the tar absorption tower provided in the downstream is supplied into the above alkali absorption furnace. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种气化系统,其使用气化炉来利用生物质,垃圾,下水道污泥等的有机资源和煤等作为烃类固体燃料,可以有效地使用 由下游设置的焦油吸收塔引出的活性炭,并且可以通过促进气化炉内的炭的气化来实现综合气化效率。 解决方案:使用气化反应炉进行烃类固体燃料的气化系统,并且设置有碱吸收炉,用于将烃类固体燃料热分解时的碱蒸发到炭上 使用用于使从上述碱性吸收炉引入的炭气化的气化炉,以及通过燃烧从上述气化炉引入的残留焦炭产生可燃性气体的燃烧炉,其中的每一个通过连通 通道,其特征在于从设置在下游的焦油吸收塔引出的活性炭被供给到上述碱吸收炉中。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Method for generating combustible gas and gasification reaction furnace therefor
    • 用于生成可燃气体和气体反应炉的方法
    • JP2008303377A
    • 2008-12-18
    • JP2008042698
    • 2008-02-25
    • National Institute Of Advanced Industrial & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHIKURAMOTO KOJISUZUKI ZENZO
    • C10J3/00C10J3/02C10J3/46
    • PROBLEM TO BE SOLVED: To provide a method efficiently taking out combustible gas, in a method and device adapted to use organic resource (biomass, garbage, sewage sludge, etc.), coal or the like as a hydrocarbon-based solid fuel and taking out it as combustible gas by promoting gasification of char-rich fuel at low temperature, thereby increasing the amount of combustible gas which can be taken in a gasification furnace, and a gasification reaction furnace therefor. SOLUTION: An alkali absorption furnace for actively adsorbing alkali and/or alkaline earth metal vaporized during thermal decomposition of the hydrocarbon-based solid fuel such as organic resources or coal to the char, a gasification furnace for gasifying the char introduced from the alkali absorption furnace, and a combustion furnace for burning the residual char introduced from the gasification furnace to generate combustion gas are independently provided. According to this, the alkali and/or alkaline earth metal that are effective as catalyst can be actively adsorbed to the char within the alkali absorption furnace and used, whereby combustible gas can be efficiently produced. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了提供一种有效地取出可燃气体的方法,在适于使用有机资源(生物质,垃圾,污水污泥等),煤等作为烃基固体的方法和装置中 燃料,并通过促进低温下富含焦油的燃料的气化将其作为可燃气体取出,从而增加在气化炉中可以采取的可燃气体的量,以及气化反应炉。 解决方案:一种碱性吸收炉,用于主动吸附碱性和/或碱土金属在烃类固体燃料如有机资源或煤炭的热分解过程中汽化,将炭化气化气化气化炉 碱性吸收炉和用于燃烧从气化炉引入的残留焦炭以产生燃烧气体的燃烧炉。 因此,作为催化剂有效的碱土金属和/或碱土金属可以积极地吸附在碱吸收炉内的炭上并被使用,由此可以有效地制造可燃气体。 版权所有(C)2009,JPO&INPIT
    • 6. 发明专利
    • Circulating fluidized bed gasification reactor enabling to effectively use tar adsorptive substance
    • 循环流化床加气反应器,有效地使用TAR吸附物质
    • JP2011105892A
    • 2011-06-02
    • JP2009264485
    • 2009-11-20
    • National Institute Of Advanced Industrial Science & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHISUZUKI ZENZO
    • C10J3/54C10J3/56
    • PROBLEM TO BE SOLVED: To provide a circulating fluidized bed gasification reactor enabling to effectively use a deteriorated tar adsorptive substance in a fluidized bed gasification furnace with a simple method without easily disposing of the tar adsorptive substance.
      SOLUTION: In the circulating fluidized bed gasification reactor configured such that a raw material is gasified in a fluidized bed gasification furnace into which a fluid medium is introduced, char generated during gasification and the fluid medium are introduced into a fluidized bed combustion furnace of a latter part to burn an unburned component and the reheated fluid medium is circulated in a reactor furnace, a thermal decomposition furnace having a two-stage structure vertically having a tar absorption furnace and a fuel thermal decomposition furnace is provided in a prior stage of the fluidized bed gasification furnace, so that the fluid medium taken out from the fuel thermal decomposition furnace of a lower stage and containing unburned char and a fluid medium taken out from the tar absorption furnace of an upper stage and adsorbing tar can be respectively independently circulated, and a communicating path connecting to a side surface of the tar absorption furnace and a side surface of the fuel thermal decomposition furnace is provided so that the fluid medium adsorbing tar in the tar absorption furnace of the upper stage can be supplied to the fuel thermal decomposition furnace of the lower stage when the deteriorated fluid medium is taken out from the fuel thermal decomposition furnace.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种循环流化床气化反应器,其能够以简单的方法在流化床气化炉中有效地使用劣化的焦油吸附物质,而不容易处理焦油吸附物质。 解决方案:在循环流化床气化反应器中,将原料气化在流化床气化炉中,其中引入流体介质,气化过程中产生的焦炭和流体介质被引入流化床燃烧炉 的后部燃烧未燃烧组分,并且再热流体介质在反应炉中循环,在具有焦油吸收炉和燃料热分解炉的垂直方向上具有两级结构的热分解炉设置在 流化床气化炉,从下段的燃料热分解炉中取出的含有未燃焦炭的液体介质和从上段的焦油吸收炉取出的流体介质和吸附焦油可分别独立循环 以及连接到焦油吸收炉的侧面和侧面的连通路径 提供燃料热分解炉的表面,使得当将劣化的流体介质从燃料热中取出时,能够向上级的焦油吸收炉吸附焦油的流体介质供应到下级的燃料热分解炉 分解炉 版权所有(C)2011,JPO&INPIT
    • 7. 发明专利
    • Circulating fluidized bed gasification reaction furnace
    • 循环流化床气化反应炉
    • JP2011037933A
    • 2011-02-24
    • JP2009183958
    • 2009-08-07
    • National Institute Of Advanced Industrial Science & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHIKURAMOTO KOJISUZUKI ZENZO
    • C10J3/54C10J3/56
    • PROBLEM TO BE SOLVED: To provide a circulating fluidized bed gasification reaction furnace wherein a usage amount of a tar adsorbing substance such as porous particles used as a fluid medium is reduced as much as possible, the fluid medium is circulated without being intermingled with ash particles and costs for tar treatment can be reduced.
      SOLUTION: In the circulating fluidized bed gasification reaction furnace wherein a raw material is gasified in a fluidized bed gasification furnace in which the fluid medium is introduced, char generated upon gasification and the fluid medium are introduced to a fluidized bed burning furnace of a latter part to burn an unburned part and the re-heated fluid medium is circulated in the reaction furnace, the fluidized bed gasification furnace is provided as a two step furnace structure vertically having a tar absorbing furnace and a fuel gasification furnace and a fluid medium taken out from the fuel gasification furnace of a lower side and containing unburned char and a fluid medium taken out from the tar absorbing furnace of an upper side and adsorbing tar are respectively independently circulated.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了提供一种循环流化床气化反应炉,其中尽可能地减少用作流体介质的诸如多孔颗粒的焦油吸附物质的使用量,使流体介质循环而不混合 灰尘颗粒和焦油处理成本可以降低。 解决方案:在循环流化床气化反应炉中,将原料气化在流化床气化炉中,其中引入流体介质,气化后产生的焦炭和流体介质被引入到流化床燃烧炉 燃烧未燃烧部分的后部分和再加热的流体介质在反应炉中循环,流化床气化炉作为垂直的两步炉结构设置,具有焦油吸收炉和燃料气化炉和流体介质 从下侧的燃料气化炉中取出含有未燃烧的焦炭和从上侧的焦油吸收炉取出的流体介质和吸附焦油分别独立地循环。 版权所有(C)2011,JPO&INPIT
    • 8. 发明专利
    • Circulating fluidized bed gasification reactor
    • 循环流化床气化反应器
    • JP2011105890A
    • 2011-06-02
    • JP2009264483
    • 2009-11-20
    • National Institute Of Advanced Industrial Science & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHISUZUKI ZENZO
    • C10J3/54B09B3/00C02F11/10C10J3/00C10K1/04
    • Y02E50/30
    • PROBLEM TO BE SOLVED: To provide a gasification reactor efficiently removing up to light tar in a system with a simple method and reducing a cost for tar treatment.
      SOLUTION: In the circulating fluidized bed gasification reactor configured such that a raw material is gasified in a fluidized bed gasification furnace in which a fluid medium is introduced, char generated during gasification and the fluid medium are introduced into a fluidized bed combustion furnace of a latter part to burn an unburned component and the reheated fluid medium is circulated in a reactor furnace, multi-stage cyclones are provided at a latter part of the fluidized bed combustion furnace, tar adsorptive particles and/or ash particles having comparatively large particle diameter are discharged out of the furnace by the first-stage cyclone and separated from an exhaust gas by the second-stage or latter cyclones.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种气化反应器,其以简单的方法有效地除去系统中的轻焦油并降低焦油处理的成本。 解决方案:在循环流化床气化反应器中,在引入流体介质的流化床气化炉中气化原料,气化过程中产生的焦炭和流体介质被引入流化床燃烧炉 的后部燃烧未燃烧组分,并且再热流体介质在反应炉中循环,在流化床燃烧炉的后部提供多级旋风分离器,具有较大颗粒的焦油吸附颗粒和/或灰分颗粒 直径通过第一级旋风分离器排出炉外,并通过第二级或后级旋风分离器与废气分离。 版权所有(C)2011,JPO&INPIT
    • 9. 发明专利
    • Circulating fluidized bed gasification furnace structure
    • 循环流化床气化炉结构
    • JP2011026491A
    • 2011-02-10
    • JP2009175252
    • 2009-07-28
    • National Institute Of Advanced Industrial Science & Technology独立行政法人産業技術総合研究所
    • MURAKAMI TAKAHIROMATSUOKA KOICHISUZUKI ZENZO
    • C10J3/54C10J3/56
    • PROBLEM TO BE SOLVED: To provide a circulating fluidized bed gasification furnace reducing the amount used of porous fine particles having the preferable adsorption efficiency of tar as little as possible without allowing the porous fine particles to coexist with ash particles and further improving gasification efficiency in a gasification furnace with a convenient technique.
      SOLUTION: The circulating fluidized bed gasification furnace is configured such that raw material is gasified in the fluidized bed gasification furnace to which a fluidizing medium is introduced, char produced upon gasification and the fluidizing medium are introduced to a fluidized bed combustion furnace of a subsequent step to combust an uncombusted content and, at the same time, the reheated fluidized medium is circulated in a reaction furnace, wherein a pyrolysis furnace of a two-stage furnace structure having a tar absorption furnace and a fuel pyrolysis furnace respectively on the upper and lower sides is disposed on a precedent step of the fluidized bed gasification furnace, a char gasification furnace and a char residue combustion furnace are connected in the order on a subsequent step of the lower stage, a coke gasification furnace and a coke residue combustion furnace are connected in the order on a subsequent step of the tar absorption furnace of the upper stage and, at the same time, a separate gasifying agent introduction means is disposed on each of the char gasifying furnace and the coke gasifying furnace.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:为了提供循环流化床气化炉,尽可能少地减少具有优选的焦油吸附效率的多孔微粒的使用量,而不允许多孔细颗粒与灰分颗粒共存并进一步改善气化 气化炉的效率方便。 解决方案:循环流化床气化炉被配置成使原料在流化床气化炉中被气化,流化床气化炉中引入流化介质,气化产生的焦炭和流化介质被引入流化床燃烧炉 燃烧未燃烧的内容物的后续步骤,同时将再加热的流化介质在反应炉中循环,其中分别具有焦油吸收炉和燃料热解炉的两级炉结构的热解炉 上下两侧设置在流化床气化炉的先行步骤中,焦化气化炉和焦炭残留燃烧炉依次连接在下一级的后续步骤,焦炭气化炉和焦炭残留燃烧 炉子在上段的焦油吸收炉的后续步骤和t的顺序连接 同时,在焦炭气化炉和焦炭气化炉的每一个上设置单独的气化剂引入装置。 版权所有(C)2011,JPO&INPIT