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    • 2. 发明专利
    • Method for manufacturing solid fuel and solid fuel manufactured by the method
    • 方法制造固体燃料和固体燃料的方法
    • JP2010235959A
    • 2010-10-21
    • JP2010167295
    • 2010-07-26
    • Kobe Steel Ltd株式会社神戸製鋼所
    • YAMAMOTO SEIICHISHIGEHISA TAKUOMIFUJI YUTAKASUGITA SATORUKINOSHITA SHIGERU
    • C10L5/00C10L5/04C10L9/08C10L9/10
    • PROBLEM TO BE SOLVED: To provide a method for manufacturing a modified solid fuel for lowering manufacturing cost and an environmental load, increasing strength for conveyance and the like, and suppressing spontaneous ignition, and to provide the modified solid fuel manufactured by the method.
      SOLUTION: The solid fuel is manufactured by grinding low grade coal, mixing a solvent oil component with the ground low grade coal to prepare slurry, heating the slurry to a temperature equal to or higher than a boiling point of water to vaporize water contained in the slurry, separating the solvent oil component from the slurry to form coal powder, and compressing and molding the coal powder. In manufacturing the solid fuel, a nonvolatile component contained in the low grade coal is extracted by the solvent oil component when the slurry is heated to the temperature equal to or higher than the boiling point of water, and the outer surface of the low grade coal and the inner surface of its pore are coated with the extracted nonvolatile component, while a content of a heavy oil component added externally is set to be lower than 0.5 mass%, preferably substantially 0%, to the dried solid fuel.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种用于制造改性固体燃料以降低制造成本和环境负荷的方法,提高输送强度等并抑制自发点火,并提供由本发明制造的改性固体燃料 方法。

      解决方案:固体燃料是通过研磨低等级煤,将溶剂油组分与低等级低级煤混合来制备浆料,将浆料加热到等于或高于沸点的水蒸发水 将浆料中的溶剂油成分从浆料中分离而形成煤粉,并压缩和成型煤粉。 在固体燃料的制造中,当将浆料加热至等于或高于沸点的温度,低等级煤的外表面时,低等级煤中所含的不挥发成分被溶剂油组分萃取 将其外部的重油成分的含量设定为干燥的固体燃料的0.5质量%以下,优选为基本上为0%。 版权所有(C)2011,JPO&INPIT

    • 3. 发明专利
    • Control method of vapor temperature of vapor compressor in upgraded brown coal process
    • 蒸馏器压缩机蒸发温度控制方法
    • JP2010053174A
    • 2010-03-11
    • JP2008216778
    • 2008-08-26
    • Kobe Steel Ltd株式会社神戸製鋼所
    • KINOSHITA SHIGERUYAMAMOTO SEIICHISUGITA SATORUMIFUJI YUTAKASHIGEHISA TAKUO
    • C10L5/00F22G5/12
    • Y02E50/30
    • PROBLEM TO BE SOLVED: To provide a control method of the vapor temperature of a vapor compressor in an upgraded brown coal process capable of controlling the temperature of a process vapor.
      SOLUTION: This control method of the vapor temperature is one of the vapor temperature of a vapor compressor 20 comprising: supplying a supply process vapor to a vapor compressor 20 to supply the resultant heated and pressurized compressed process vapor to an evaporator 27 as a heating source of the evaporator; and cooling down the residual compressed process vapor by pouring water from a water supply source through a water pouring line 29 before returning the compressed process vapor through a super-heated vapor supply line 25 to a process vapor supply line 22 in which: water is poured to the compressed process vapor through a plurality of points having pouring flow rates different from each other so that a calorie calculated from the temperature and flow rate of a mixed vapor comprising a compressed process vapor and a steam after pouring water to the compressed process vapor becomes equal to the sum of a calorie calculated from the temperature and flow rate of the compressed process vapor and a calorie calculated from the temperature and flow rate of the poured water; and at least one point among the plurality of points is always used and the amount of water shared to other pouring points is controlled corresponding to the pouring water flow rate.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供能够控制工艺蒸汽的温度的升级的褐煤过程中的蒸气压缩机的蒸汽温度的控制方法。 蒸汽温度的这种控制方法是蒸气压缩机20的蒸汽温度之一,其包括:向蒸气压缩机20供应供应过程蒸汽,以将所得加热和加压的压缩过程蒸气供应到蒸发器27,作为 蒸发器的加热源; 以及通过从供水源倾倒水通过注水管线29将所述压缩过程蒸汽返回到过热蒸汽供应管线22之前将所述压缩过程蒸气返回到过程蒸汽供应管线22中来冷却残余的压缩过程蒸汽,其中:浇注水 通过具有彼此不同的倾倒流速的多个点对压缩过程蒸气,使得在将水倒入压缩过程蒸气后,包括压缩过程蒸汽和蒸汽的混合蒸汽的温度和流速计算出的卡路里变成 等于从压缩过程蒸汽的温度和流速计算出的热量和从倾倒的水的温度和流量计算的卡路里的总和; 并且总是使用多个点中的至少一个点,并且根据倾倒水流量来控制与其他倾倒点共享的水量。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • Gas separation method and gas separation apparatus
    • 气体分离方法和气体分离装置
    • JP2009023907A
    • 2009-02-05
    • JP2008230055
    • 2008-09-08
    • Kobe Steel Ltd株式会社神戸製鋼所
    • YAMAMOTO SEIICHIYURA KEITA
    • C01B32/40B01D53/04
    • PROBLEM TO BE SOLVED: To obtain a product gas having higher purity in the case when the product gas is separated and recovered through adsorption onto an adsorbent. SOLUTION: A raw material gas containing carbon monoxide is supplied into adsorption columns 16A, 16B and thereafter, carbon monoxide is separated and recovered by desorbing carbon monoxide from an adsorbent. At this time, the pressure of the adsorption columns 16A, 16B is reduced by an ejector 18 operated with steam as a primary fluid (driving fluid) and carbon monoxide (secondary fluid) desorbed from the adsorbent is discharged together with steam (primary fluid) while being sucked into the ejector 18. Then, the discharged fluids are cooled to an ordinary temperature or near to the ordinary temperature to condense steam. The discharged fluids are thereby vapor-liquid separated and carbon monoxide being a gas component is recovered as the product gas. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:在通过吸附分离和回收产物气体的情况下获得具有较高纯度的产物气体。 解决方案:将含有一氧化碳的原料气体供应到吸附塔16A,16B中,此后通过从吸附剂中解吸一氧化碳来分离和回收一氧化碳。 此时,吸附塔16A,16B的压力由作为主要流体(驱动流体)的蒸汽操作的喷射器18减少,并且从吸附剂解吸的一氧化碳(二次流体)与蒸汽(主要流体)一起排出, 同时被吸入喷射器18.然后,排出的流体被冷却到常温或接近常温以冷凝蒸汽。 排出的流体由此气液分离,作为气体成分的一氧化碳作为产物气体被回收。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Flow path structure, reactor, and method of reacting using reactor
    • 流动路径结构,反应器和使用反应器的反应方法
    • JP2009018280A
    • 2009-01-29
    • JP2007184302
    • 2007-07-13
    • Kobe Steel Ltd株式会社神戸製鋼所
    • NOISSHIKI KOJIYOSHIDA TATSUOYAMAMOTO SEIICHIOKADA KAZUTO
    • B01J19/00F28D9/00G01N35/08
    • PROBLEM TO BE SOLVED: To improve degrees of freedom for a shape of each flow path while uniformizing a flow volume of a fluid which flows through each flow path.
      SOLUTION: Each reaction flow path 2 of a first flow path structure 1a includes: a first introducing path 10 introducing a first raw material fluid; a second introducing path 12 introducing a second raw material fluid; a converging part 14 connected to the downstream sides of the first introducing path 10 and the second introducing path 12 and converging the first raw material fluid and the second raw material fluid; and a reaction path 16 connected to the downstream side of the converging part 14 for reacting the first raw material fluid and the second raw material fluid. While the flow path length of the second introducing path 12 of each reaction flow path 2 is different from each other, a diameter corresponding to each part of each second introducing path 12 is set according to the flow path length of each second introducing path 12 so as to equalize each other a whole pressure loss of each second introducing path 12.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:为了改善每个流动路径的形状的自由度,同时使流过每个流动路径的流体的流量均匀化。 解决方案:第一流路结构1a的每个反应流路2包括:引入第一原料流体的第一引入路径10; 引入第二原料流体的第二引入路径12; 与第一导入路径10和第二导入路径12的下游侧连接并会聚第一原料流体和第二原料流体的收敛部14; 以及连接到会聚部14的下游侧的反应路径16,用于使第一原料流体和第二原料流体反应。 当反应流路2的第二导入路径12的流路长度彼此不同时,根据第二导入路径12的流路长度设定与第二导入路径12的各部分对应的直径, 以便彼此平衡每个第二引入路径12的整体压力损失。版权所有:(C)2009,JPO&INPIT
    • 6. 发明专利
    • Reaction apparatus and reaction method
    • 反应装置和反应方法
    • JP2008168173A
    • 2008-07-24
    • JP2007001120
    • 2007-01-09
    • Kobe Steel Ltd株式会社神戸製鋼所
    • BAN HIROYUKINOISSHIKI KOJIOKADA KAZUTOYAMAMOTO SEIICHI
    • B01J19/00
    • PROBLEM TO BE SOLVED: To more enhance reaction efficiency by increasing the contact areas per unit volume of both first and second reactants without contracting the dimensions in the layer thickness of the introducing passages of the first and second reactants.
      SOLUTION: In this reaction apparatus, a flow channel 4a includes: a first introducing passage 10 into which the first reactant is introduced; a second introducing passage 12 into which the second reactant is introduced; a confluent passage 14 for allowing the first reactant flowing through the introducing passage 10 and the second reactant flowing through the second introducing passage 12 to meet with each other in a mutually separated layered flow state; and the reaction flow passage 16 connected to the confluent passage 14 on the downstream side thereof for allowing the layered flow of the first reactant and the layered flow of the second reactant to flow in the mutual contact state of both reactants to react both reactants in the mutual contact interface of them. The dimension d3 in the layer thickness direction vertical to the contact interface of the reaction flow channel 16 is set to become smaller than the sum of the dimension d1 in the layer thickness direction of the first introducing passage 10 and the dimension d2 in the layer thickness direction of the second introducing passage 12.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:通过增加第一和第二反应物的每单位体积的接触面积而不会缩小第一和第二反应物的引入通道的层厚度的尺寸,来提高反应效率。 解决方案:在该反应装置中,流动通道4a包括:引入第一反应物的第一引入通道10; 引入第二反应物的第二引入通道12; 汇合通道14,用于允许第一反应物流过引入通道10,第二反应物流过第二引入通道12以相互分离的分层流动状态彼此相遇; 和反应流路16连接到下游侧的汇合通道14,以使第一反应物的层流和第二反应物的层流在两种反应物的相互接触状态下流动,以使两种反应物在 它们的相互接触界面。 与反应流路16的接触界面垂直的层厚方向的尺寸d3设定为小于第一导入通道10的层厚度方向的尺寸d1和层厚度的尺寸d2之和 第二引入通道12的方向。(C)2008,JPO&INPIT
    • 9. 发明专利
    • Iodine separation method
    • 碘分离方法
    • JP2008051536A
    • 2008-03-06
    • JP2006225412
    • 2006-08-22
    • Kobe Steel Ltd株式会社神戸製鋼所
    • KINOSHITA SHIGERUYAMAMOTO SEIICHIMASUDA KAORUWADA RYUTAROKATO OSAMU
    • G21F9/30G21F9/02
    • PROBLEM TO BE SOLVED: To provide a useful method capable of separating iodine effectively, while reducing back end cost, when separating iodine from a radioactive iodine including silver compound discharged from a nuclear power industry facility such as a nuclear power plant or a nuclear fuel reprocessing factory.
      SOLUTION: When separating iodine from a compound including radioactive iodine and silver, a reaction agent is reacted with the compound in a system including a surfactant and comprising a continuous phase and a water phase as a dispersed phase, and hereby iodine in the compound is solubilized into the water phase, to separate iodine.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种能够有效地分离碘,同时降低后端成本的有用方法,当将碘从包括从诸如核电站或核电厂的核电工业设施排出的银化合物的放射性碘分离时, 核燃料后处理厂。 解决方案:当从包括放射性碘和银在内的化合物分离碘时,将反应剂与包含表面活性剂的系统中的化合物反应,并且包含作为分散相的连续相和水相,因此在 化合物溶解到水相中,以分离碘。 版权所有(C)2008,JPO&INPIT
    • 10. 发明专利
    • Catalyst for reforming methanol with steam and method for preparing the same
    • 用于用蒸汽重整甲醇的催化剂及其制备方法
    • JP2007268453A
    • 2007-10-18
    • JP2006098599
    • 2006-03-31
    • Kobe Steel Ltd株式会社神戸製鋼所
    • MATSUBARA MASAAKIYAMAMOTO SEIICHIYAMASHITA TAKESHIFUJISAWA AKITOSHI
    • B01J23/80B01J37/02C01B3/32H01M8/06
    • Y02E60/50
    • PROBLEM TO BE SOLVED: To provide a catalyst for reforming methanol with steam comprised of a catalyst component comprising copper and zinc uniformly supported by the surface of a metal in a large amount, and a method for preparing the same. SOLUTION: The catalyst 1 for reforming methanol with steam is prepared by forming a first plating layer formed by electroless plating of zinc on the surface of a metal plate, a metal cylinder, or a metal pipe, a second plating layer formed by flash plating of copper directly on the first plating layer, and a third plating layer formed by electroless plating of copper directly on the second plating layer, and subsequently exposing the above zinc and copper on the surface of the plated article by subjecting the same to a calcination treatment. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种用于由包含铜和锌的催化剂组分的蒸汽重整甲醇的催化剂,所述催化剂组分由金属的表面均匀地被大量支撑,及其制备方法。 解决方案:用蒸汽重整甲醇的催化剂1通过在金属板,金属圆筒或金属管的表面上形成通过无电镀锌形成的第一镀层来制备,第二镀层由 直接在第一镀层上直接镀铜,以及通过在第二镀层上直接化学镀铜而形成的第三镀层,然后通过将镀锌物品的表面上的锌和铜暴露于镀层 煅烧处理。 版权所有(C)2008,JPO&INPIT