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    • 1. 发明专利
    • Apparatus for producing nanocarbon
    • 生产纳米碳的装置
    • JP2012041270A
    • 2012-03-01
    • JP2011265097
    • 2011-12-02
    • Toshiba Corp株式会社東芝
    • IDE KATSUNORIKOSHIRO KAZUTAKASUGIYAMA HIDEKAZUNOMA TAKESHI
    • C01B31/02
    • PROBLEM TO BE SOLVED: To efficiently mass-produce highly functional nanocarbon having high purity and stability at low cost.SOLUTION: An apparatus for producing nanocarbon includes: a reactor 1 the inside of which can be kept in a reducing atmosphere; an endless belt-like iron sheet 3 which is disposed in the reactor, driven by rollers and subjected to the formation of CNT (carbon nanotube) 2 on a surface thereof; a heater 4 which heats the belt-like iron sheet; a hydrocarbon feeding unit 5 to feed a hydrocarbon into the reactor; an inert gas-feeding unit 6 to feed an inert gas into the reactor; a recovery unit 7 to recover CNT formed on the belt-like iron sheet; and a gas exhaust unit 9 to exhaust the gas in the reactor.
    • 要解决的问题:以低成本有效地批量生产具有高纯度和稳定性的高功能纳米碳。 解决方案:一种用于生产纳米碳的设备包括:反应器1,其内部可以保持在还原气氛中; 设置在反应器中,由辊驱动并在其表面上形成CNT(碳纳米管)2的环状带状铁片3; 加热器4,其加热带状铁片; 烃进料单元5,用于将烃进料到反应器中; 惰性气体供给单元6,用于将惰性气体进料到反应器中; 回收单元7,用于回收形成在带状铁片上的CNT; 和排气单元9,以排出反应器中的气体。 版权所有(C)2012,JPO&INPIT
    • 2. 发明专利
    • Pyrolizing furnace system
    • 热解炉系统
    • JP2010139219A
    • 2010-06-24
    • JP2008318715
    • 2008-12-15
    • Toshiba Corp株式会社東芝
    • IDE KATSUNORIHAYASHI KOJISUGIYAMA HIDEKAZUKOMINE HIDEAKI
    • F27B7/04B09B3/00C10B53/00F27B7/08F27B7/16F27B7/30F27B7/42
    • PROBLEM TO BE SOLVED: To stably continue pyrolysis treatment throughout a long period of time by preventing progress of adhesion of deposits on an inner face of a revolving drum.
      SOLUTION: In the pyrolizing furnace system of a transverse external heating rotating type, a treatment reception object is heated and pyrolized in a reductive atmosphere, and it is separated into pyrolysis gas and pyrolysis residues mainly composed of nonvolatile components. A partition disc 21 allowing only passage of cracked gas and residues is provided in an interior of the revolving drum 14, and of a precedent pyrolysis chamber 22 and a posterior pyrolysis chamber 23 partitioned by the partition disc 21, a ball 24 and a scraping blade 25 are provided in the precedent pyrolysis chamber 22.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:通过防止沉积物在旋转滚筒的内表面上的附着进行,在长时间内稳定地继续热解处理。 解决方案:在横向外部加热旋转式的热解炉系统中,将处理接收物体在还原气氛中加热和热解,并将其分离成主要由非挥发性组分组成的热解气体和裂解残渣。 在旋转滚筒14的内部和先前的热解室22和由分隔盘21分隔的后部热解室23的内部设置有仅允许裂解气体和残留物通过的分隔盘21,球24和刮板 25在先前的热解室22中提供。版权所有(C)2010,JPO&INPIT
    • 3. 发明专利
    • Nanocarbon and carbonized material continuous production apparatus
    • 纳米碳和碳化物连续生产设备
    • JP2009242179A
    • 2009-10-22
    • JP2008091725
    • 2008-03-31
    • Toshiba Corp株式会社東芝
    • SUGIYAMA HIDEKAZUNOMA TAKESHIIDE KATSUNORIIMAI TADASHIKOSHIRO KAZUTAKA
    • C01B31/02C01B31/08
    • PROBLEM TO BE SOLVED: To continuously produce not only highly functional nanocarbon but also carbonized materials such as activated carbon without using energy of fossil resource origin in the formation of highly functional nanocarbon such as a carbon nanotube, and to collectively and stably produce highly functional nanocarbon, carbonized materials such as activated carbon, wood vinegar, etc., while continuously feeding organic matter treated materials. SOLUTION: A nanocarbon and carbonized material continuous production apparatus is provided with a first-stage drying means 1 to dry a first organic matter treated material, a middle-stage carbonization and pyrolytic liquid recovery means 2 to carbonize and pyrolyze the dried first organic matter treated material and to recover the resultant pyrolytic liquid, and a latter-stage nanocarbon formation means 3 to form nanocarbon from the recovered pyrolytic liquid, wherein a dried second organic matter treated material different from the first organic matter treated material fed into the first-stage drying means 1 is fed into the middle-stage carbonization and pyrolytic liquid recovery means 2, thereby nanocarbon and carbonized materials are continuously produced from the first and the second organic matter treated materials. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:为了连续地生产高功能性纳米碳,而且不断地生产活性炭等碳化材料,而不需要化石能源来形成碳纳米管等高功能性纳米碳,并且能够共同稳定地生产 高功能纳米碳,碳化材料如活性炭,木醋等,同时连续喂食有机物处理材料。 解决方案:纳米碳碳化材料连续制备装置设置有干燥第一有机物处理材料的第一阶段干燥装置1,中间阶段碳化和热解液回收装置2,以将干燥的第一干燥装置碳化和热解 有机物处理材料并回收所得的热解液,以及后期纳米碳形成装置3,用于从回收的热解液中形成纳米碳,其中干燥的第二有机物质处理材料与第一有机物处理材料不同, 阶段干燥装置1被供给到中间阶段碳化和热解液回收装置2中,由此从第一和第二有机物处理材料连续地生产纳米碳和碳化材料。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • Carbon nanotube production furnace
    • 碳纳米管生产炉
    • JP2009120413A
    • 2009-06-04
    • JP2007293585
    • 2007-11-12
    • Toshiba Corp株式会社東芝
    • IDE KATSUNORIKOSHIRO KAZUTAKASUGIYAMA HIDEKAZUNOMA TAKESHIIMAI TADASHI
    • C01B31/02B01J8/12
    • PROBLEM TO BE SOLVED: To provide a carbon nanotube production furnace which realizes the low cost and efficient mass production of carbon nanotubes of high purity, stability and performance.
      SOLUTION: The carbon nanotube production furnace has a vertical heating furnace vessel 11 kept in a reducing atmosphere, metal balls 12 packed inside of the heating furnace vessel 11, a heater 13 arranged outside of the heating furnace vessel 11, a shelf 14 which is arranged within the heating furnace vessel 11 and holds the metal balls 12 and having communicated holes through which a metal powder catalyst and gas pass, agitation blades 16 agitating the metal balls 12 and a feed means with which the metal powder catalyst and a raw material hydrocarbon are fed.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 解决的问题:提供一种实现高纯度,稳定性和性能的碳纳米管的低成本和高效批量生产的碳纳米管制造炉。 解决方案:碳纳米管生产炉具有保持在还原气氛中的垂直加热炉容器11,装在加热炉容器11内的金属球12,设置在加热炉容器11外部的加热器13,搁板14 其布置在加热炉容器11内并保持金属球12并具有通过金属粉末催化剂和气体通过的连通孔,搅拌叶片16搅拌金属球12和进料装置,金属粉末催化剂和原料 原料烃进料。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Thermal decomposition oil recovery system
    • 热分解油回收系统
    • JP2008297470A
    • 2008-12-11
    • JP2007145896
    • 2007-05-31
    • Toshiba Corp株式会社東芝
    • SUGIYAMA HIDEKAZUIMAI TADASHINOMA TAKESHIKOSHIRO KAZUTAKA
    • C10G1/10B09B3/00C10G1/00
    • Y02E50/30Y02W30/20
    • PROBLEM TO BE SOLVED: To solve the problem that in conventional methods fractionating recovered thermal decomposition oil obtained by thermal decomposition of a mixture of organic materials, depending on the characters the system tends to be a complicated system. SOLUTION: The thermal decomposition oil recovery system which recovers thermally decomposed oil from generated thermally decomposed gas, comprises a first step thermal decomposition oil recovery loop 12 having a thermal decomposition gas ejector 14a condensing the thermal decomposition gas generated by thermally decomposing mixed organic materials with a recovered decomposition oil, a decomposed oil tank 15a storing the condensed thermal decomposition oil, and a decomposition oil coolor 18a for cooling the condensed thermally decomposed oil, and a second step thermal decomposition oil recovering loop 13 having a thermal decomposition gas ejector 14b condensing the thermal decomposition gas which could not be condensed by the thermal decomposition gas ejector with the decomposition oil, a decomposition oil tank 15b storing the condensed thermally decomposed oil condensed by the gas ejector and a decomposition oil cooler 18b cooling the thermally decomposed oil. COPYRIGHT: (C)2009,JPO&INPIT
    • 解决的问题:为了解决在以往的方法中,通过有机物质的混合物的热分解而得到的回收热分解油的分馏,系统倾向于是复杂的系统。 解决方案:从产生的热分解气体中回收热分解油的热分解油回收系统包括第一级热分解油回收回路12,其具有热分解气体喷射器14a,其冷凝通过热分解混合有机物产生的热分解气体 具有回收的分解油的材料,存储冷凝的热分解油的分解油箱15a和用于冷却冷凝的热分解油的分解油冷却器18a和具有热分解气体喷射器14b的第二阶段热分解油回收回路13 冷凝热分解气体喷射器不能与分解油冷凝的热分解气体,储存由气体喷射器冷凝的冷凝热分解油的分解油箱15b和冷却热分解油的分解油冷却器18b。 版权所有(C)2009,JPO&INPIT
    • 7. 发明专利
    • Heating oven for waste plastic decomposition oil
    • 加热炉用于废塑料分解油
    • JP2008189913A
    • 2008-08-21
    • JP2008001252
    • 2008-01-08
    • Toshiba Corp株式会社東芝
    • SUGIYAMA HIDEKAZU
    • C10G1/10
    • PROBLEM TO BE SOLVED: To provide a heating oven for a waste plastic decomposition oil which can effectively prevent the blocking of a pipe for a condensation oil when the pipe comprises two kinds of pipes different in diameter.
      SOLUTION: The heating oven for the waste plastic decomposition oil is for heating a waste plastic decomposition oil obtained by condensing an oil gas obtained by thermally decomposing a waste plastic, wherein the oven is equipped with a first pipeline 21, into which the condensed waste plastic decomposition oil is introduced, and a second pipeline 22 connected to the first pipeline 21; the first pipeline 21 and the second pipeline 22 are surrounded by an oven wall; the area surrounded by the oven wall is heated by a heating means; the diameter of the second pipeline 22 is larger than that of the first pipeline 21; and different pigs can be driven into the pipelines 21 and 22.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供用于废塑料分解油的加热炉,当管道包括直径不同的两种管道时,可有效地防止冷凝油管道堵塞。 解决方案:废塑料分解油的加热炉用于加热通过冷凝通过热分解废塑料获得的油气而获得的废塑料分解油,其中炉子装备有第一管道21,其中 引入冷凝废塑料分解油,连接到第一管道21的第二管道22; 第一管道21和第二管道22被炉壁包围; 由炉壁包围的区域被加热装置加热; 第二管道22的直径大于第一管道21的直径; 并且不同的猪可以被驱入管道21和22。版权所有:(C)2008,JPO&INPIT
    • 8. 发明专利
    • Method for producing carbon nanotube
    • 生产碳纳米管的方法
    • JP2008100869A
    • 2008-05-01
    • JP2006284233
    • 2006-10-18
    • Toshiba Corp株式会社東芝
    • SUGIYAMA HIDEKAZUKOSHIRO KAZUTAKAIMAI TADASHINOMA TAKESHIYASUI SUKEYUKITANAKA MOTOFUMI
    • C01B31/02
    • PROBLEM TO BE SOLVED: To stabilize the growth of a carbon nanotube by eliminating a carbon material excluding the carbon nanotube and/or defective crystal parts of a carbon nanotube or by uniformalizing a hydrocarbon mixture to lower molecular weights.
      SOLUTION: In the method for producing a carbon nanotube using a catalytic growth method, reaction active species are generated by electric-discharging in a reaction tube 12 while carbon nanotube 18 is in the process of growing. The carbon material excluding the generated carbon nanotube 18 and/or defective crystal parts of the carbon nanotube 18 are eliminated by the generated reaction species.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:通过除去碳纳米管之外的碳材料和/或碳纳米管的有缺陷的晶体部分或通过使烃混合物均匀化以降低分子量来稳定碳纳米管的生长。 解决方案:在使用催化生长方法制备碳纳米管的方法中,反应活性物质通过在反应管12中进行放电而产生,同时碳纳米管18处于生长过程中。 通过所生成的反应物质,除去生成的碳纳米管18以外的碳材料和/或碳纳米管18的有缺陷的晶体部分。 版权所有(C)2008,JPO&INPIT
    • 9. 发明专利
    • Pyrolytic treatment apparatus
    • 热解处理装置
    • JP2007332220A
    • 2007-12-27
    • JP2006163887
    • 2006-06-13
    • Toshiba Corp株式会社東芝
    • SUGIYAMA HIDEKAZUKOSHIRO KAZUTAKANOMA TAKESHIIMAI TADASHI
    • C10G1/10B01J19/00B09B3/00C02F11/10C08J11/12C10B53/02C10B53/07C10G1/00
    • Y02E50/14Y02P20/124Y02P20/143Y02W10/40Y02W30/703
    • PROBLEM TO BE SOLVED: To provide a pyrolytic treatment apparatus which can efficiently transmit heat added from the outside to charged organic treating materials, hardly clogs portions for discharging a pyrolysis gas and residues, and can continuously treat the organic treating materials. SOLUTION: This pyrolytic treatment apparatus has a pyrolysis oven 11 which comprises an inner cylinder 12 comprising a good heat-conducting material and an outer cylinder 13 for covering the outer periphery of the inner cylinder 12 through a heating space 16. Many ceramic balls 19 are disposed in the inner cylinder 12, and the organic treating materials charged from one side of the inner cylinder 12 are thermally pyrolyzed with the heat of the heating space 16 to produce a pyrolysis gas and residues. A plurality of slits 32 are formed in a product-discharging member 31 covering the other end portion of the inner cylinder 12, and the pyrolysis gas and the pyrolysis residues produced in the inner cylinder 12 are discharged into a discharging portion box 33. The pyrolysis gas is exhausted from the box 33 through a pyrolysis gas-exhausting device 35, and the pyrolysis residues are discharged from a residue-discharging device 36. COPYRIGHT: (C)2008,JPO&INPIT
    • 待解决的问题:为了提供一种可以有效地将从外部添加的热量传递给带电有机处理材料的热解处理装置,几乎不堵塞用于排出热解气体和残余物的部分,并且可以连续处理有机处理材料。 解决方案:该热解处理装置具有热解炉11,其包括内筒12,其包括良好的导热材料和外筒13,外筒13通过加热空间16覆盖内筒12的外周。许多陶瓷 球19设置在内筒12中,从内筒12的一侧填充的有机处理材料与加热空间16的热量热分解,产生热解气体和残渣。 在覆盖内筒12的另一端的产品排出构件31中形成有多个狭缝32,并且将内部气缸12中产生的热分解气体和热解残留物排出到排出部分箱33内。热分解 气体通过热解气体排出装置35从箱33排出,热解残渣从残渣排出装置36排出。(C)2008,JPO&INPIT
    • 10. 发明专利
    • Organic waste water treatment method and arrangement
    • 有机废水处理方法和布置
    • JP2007237055A
    • 2007-09-20
    • JP2006061503
    • 2006-03-07
    • Toshiba Corp株式会社東芝
    • NAGAMORI YASUHIKOASHIKAGA NOBUYUKITAMURA HIROSHISUGIYAMA HIDEKAZU
    • C02F3/28
    • Y02E50/343
    • PROBLEM TO BE SOLVED: To provide an organic waste water treatment method which prevents a decrease in treatment performance and an increase in treatment cost of methane fermentation treatment facilities by loading it with the suitable amount of water even if the fluctuation of wastewater concentration is present, and an arrangement. SOLUTION: The organic waste water treatment method anaerobically treating the organic wastewater by a methane fermentation tank 16 comprises the steps of obtaining the load of an inhibitor per the weight of a metanogen in the methane fermentation tank 16 from the weight of the metanogen in the methane fermentation tank 16, the concentration of the inhibitor for inhibiting methane fermentation and a flow rate per unit time of water to be treated flowing into this methane fermentation tank 16, determining a relation of a change in organic substance removal ratio in the methane fermentation tank of the water to be treated for each load of each inhibitor to the concentration of the above-described inhibitor when the load of this inhibitor is changed, and adjusting either or both of the load of dilution water loaded into the organic wastewater and the supply amount of this water to be treated to the methane fermentation tank 16 so as to provide the organic substance removal ratio of the methane fermentation tank 16 with a predetermined value using this relation. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种有机废水处理方法,其即使废水浓度的波动也能够通过装入适量的水来防止甲烷发酵处理设备的处理性能降低和处理成本的增加 存在和安排。 解决方案:通过甲烷发酵罐16厌氧处理有机废水的有机废水处理方法包括以下步骤:从甲烷发酵罐16的重量中获得甲烷发酵罐16中的元素重量的抑制剂的负荷 在甲烷发酵罐16中,用于抑制甲烷发酵的抑制剂的浓度和流入该甲烷发酵罐16的待处理的每单位时间的水的流量,确定甲烷中有机物质去除率的变化的关系 当该抑制剂的负荷改变时,将每种抑制剂的每种负荷处理的水的发酵罐与上述抑制剂的浓度,并且调节负载到有机废水中的稀释水的负荷或两者 向甲烷发酵罐16供给该待处理水量,以提供有机物除去率 甲烷发酵罐16使用该关系具有预定值。 版权所有(C)2007,JPO&INPIT