会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • Method and system for recovering and utilizing waste energy
    • 回收利用废物能源的方法与系统
    • JP2012067165A
    • 2012-04-05
    • JP2010212102
    • 2010-09-22
    • Japan Steel Works Ltd:TheToshiba Corp株式会社日本製鋼所株式会社東芝
    • UMEMOTO KUNIMORITAKEDA HARUNOBUNAKAMURA SATOSHIKUBO KAZUYAYAMADA KAZUYAFUKUSHIMA KIMICHIKA
    • C10L3/10C01B3/32C01B3/56
    • PROBLEM TO BE SOLVED: To recover and make effective use of waste energy having relatively low temperature.SOLUTION: A system for recovering and utilizing the waste energy includes: a steam reformer 1 for subjecting one or more of methanol, ethanol and dimethyl ether as a feed gas to steam reforming by using steam and exhaust heat; a gas mixer 3 for mixing part or all of reformed product gas produced in the steam reformer 1 with a hydrocarbon gas; and a fuel supplying unit (a mixed gas supplying pipe 3a) for supplying the mixed gas obtained by the gas mixer 3 as a fuel. A method for recovering and utilizing the waste energy includes: subjecting the one or more of methanol, ethanol and dimethyl ether to steam reforming in the steam reformer 1 by using the exhaust heat having low temperature, or at 250-450°C; mixing the part or all of the reformed product gas with the hydrocarbon gas by the gas mixer 3; and enabling the mixed gas to be supplied at the fuel supplying unit as the fuel.
    • 要解决的问题:回收和有效利用具有较低温度的废能。 解决方案:用于回收和利用废能的系统包括:蒸汽重整器1,用于使一种或多种甲醇,乙醇和二甲醚作为进料气体通过使用蒸汽和排热进行蒸汽重整; 用于将在蒸汽重整器1中产生的重整产物气体的一部分或全部与烃气体混合的气体混合器3; 以及用于将由气体混合器3获得的混合气体作为燃料供给的燃料供给单元(混合气体供给管3a)。 回收和利用废能的方法包括:通过使用低温排气,或在250-450℃,使一种或多种甲醇,乙醇和二甲醚在蒸汽重整器1中进行蒸汽重整; 通过气体混合器3将部分或全部重整产物气体与烃气体混合; 并且能够在燃料供给单元处供给混合气体作为燃料。 版权所有(C)2012,JPO&INPIT
    • 2. 发明专利
    • Hydrogen production method and hydrogen production apparatus
    • 氢生产方法和氢生产设备
    • JP2011230939A
    • 2011-11-17
    • JP2010100492
    • 2010-04-26
    • Toshiba Corp株式会社東芝
    • YAGYU MOTOSHIGEYAMADA KAZUYAFUKUSHIMA KIMICHIKA
    • C01B3/38B01J38/06B01J38/10B01J38/18
    • Y02P20/584
    • PROBLEM TO BE SOLVED: To improve the efficiency of hydrogen production by removing hydrocarbon species adsorbed to a catalyst along with hydrogen production.SOLUTION: This hydrogen production method includes: a hydrogen production process S6 of supplying lower hydrocarbon and steam to a reaction section containing the catalyst to produce the hydrogen by the reaction of the lower hydrocarbon and the steam; a catalyst washing process S9 of washing and removing the hydrocarbon species adsorbed to a surface of the catalyst by supplying the steam and inert gas to the reaction section after the hydrogen production process S6; and a catalyst regeneration process S10 of oxidizing and removing the hydrocarbon species adsorbed to the surface of the catalyst by supplying an oxidant to the reaction section to oxidize the catalyst, and supplying a reductant to the reaction section afterwards to reduce the catalyst, after the hydrogen production process S6 and the catalyst washing process S9.
    • 要解决的问题:通过除去吸附在催化剂上的烃物质以及氢气生产来提高生产氢气的效率。 解决方案:该氢气制备方法包括:通过下部烃和蒸汽的反应向含有催化剂的反应部分供应低级烃和蒸汽以产生氢气的氢气生产方法S6; 催化剂洗涤方法S9,其通过在氢气制备过程S6之后向反应部分供应蒸汽和惰性气体来洗涤和除去吸附在催化剂表面上的烃类物质; 以及催化剂再生工序S10,通过向反应部供给氧化剂氧化除去吸附在催化剂表面的烃类,氧化催化剂,然后在还原催化剂之后向反应部供给还原剂,在氢 生产工艺S6和催化剂洗涤工艺S9。 版权所有(C)2012,JPO&INPIT
    • 3. 发明专利
    • Carbon dioxide recovery system
    • 二氧化碳回收系统
    • JP2010240629A
    • 2010-10-28
    • JP2009095678
    • 2009-04-10
    • Toshiba Corp株式会社東芝
    • IWAASA KIYOHIKOHODOZUKA MASATOSHISAKURAI MANABUYAMADA KAZUYA
    • B01D53/62B01D53/14C01B32/50
    • Y02A50/2342Y02C10/06Y02P20/124Y02P20/152Y02P20/57
    • PROBLEM TO BE SOLVED: To reduce heat energy required in an absorption liquid regeneration process in a carbon dioxide recovery system.
      SOLUTION: Between an absorption tower 3 for making an absorption liquid absorb carbon dioxide included in a combustion exhaust gas and a regeneration tower 5 for regenerating the absorption liquid supplied from the absorption tower and discharging a discharge gas containing emitted carbon dioxide gas and steam, a regenerated heat exchanger 7 is provided which heats the absorption liquid which has absorbed the carbon dioxide and supplied from the absorption tower to the regeneration tower with the regenerated absorption liquid supplied from the regeneration tower to the absorption tower as a heat source. Also, between the absorption tower and the regenerated heat exchanger or between the regenerated heat exchanger and the regeneration tower, a heat exchanger 20 is provided which heats the absorption liquid which has absorbed the carbon dioxide and supplied from the absorption tower to the regeneration tower with the discharge gas discharged from the regeneration tower as a heat source.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:减少二氧化碳回收系统中吸收液体再生过程所需的热能。 解决方案:在用于吸收液体的吸收塔3吸收包含在燃烧废气中的二氧化碳和再生塔5之间,用于再生从吸收塔供应的吸收液体并排出含有排出的二氧化碳气体的放电气体, 蒸汽,提供再生热交换器7,其将吸收了二氧化碳并从吸收塔供给的吸收液加热到再生塔,再生塔从再生塔供给到作为热源的吸收塔。 此外,在吸收塔和再生热交换器之间或再生热交换器和再生塔之间,设置有热吸收二氧化碳吸收液体并从吸收塔供给到再生塔的吸收液体的热交换器20, 从再生塔排出的放电气体作为热源。 版权所有(C)2011,JPO&INPIT
    • 6. 发明专利
    • Apparatus, system and method for producing hydrogen
    • 用于生产氢的装置,系统和方法
    • JP2008266079A
    • 2008-11-06
    • JP2007112588
    • 2007-04-23
    • Toshiba Corp株式会社東芝
    • YAMADA KAZUYAMAKINO SHINICHIYAGYU MOTOSHIGESHIGENIWA SHINOBUHARA AKIHIROFUKUSHIMA KIMICHIKA
    • C01B3/32C01B3/00C01B3/56
    • Y02E60/324
    • PROBLEM TO BE SOLVED: To efficiently produce hydrogen using dimethyl ether as a raw material at a low temperature in an easy form for storage and transportation.
      SOLUTION: The hydrogen producing apparatus is equipped with a dimethyl ether gasifier 3, a steam generator 4, a mixer 5 for forming a mixed gas 13 by mixing dimethyl ether provided from the dimethyl ether gasifier 3 and steam provided from the steam generator 4, a mixed gas preheater 6 for preheating the mixed gas 13, and a reforming separator 20. The reforming separator 20 is equipped with a steam reforming catalyst and a removably stored hydrogen occlusion material, wherein a reformed gas 22 is formed by steam reforming in contacting a preheated mixed gas 14 with the steam reforming catalyst and hydrogen contained in the reformed gas 22 is occluded into the hydrogen occlusion material by contacting the reformed gas 22 with the hydrogen occlusion material. The reforming separator 20 is equipped with a hydrogen separator 2 accommodating the hydrogen occlusion material in a detachably attached hydrogen occlusion material container.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:以容易的形式在低温下以二甲醚为原料高效地生产氢气用于储存和运输。 解决方案:制氢装置配备有二甲醚气化器3,蒸汽发生器4,用于通过混合由二甲醚气化器3提供的二甲醚和从蒸汽发生器提供的蒸汽形成混合气体13的混合器5 4,用于预热混合气体13的混合气体预热器6和重整分离器20.重整分离器20配备有蒸汽重整催化剂和可移除的储存的吸氢材料,其中通过蒸汽重整形成重整气体22 使预热的混合气体14与蒸汽重整催化剂接触,并且重整气体22中所含的氢气通过使重整气体22与吸氢材料接触而封闭到吸氢材料中。 重整分离器20配备有在可拆卸地安装的吸氢材料容器中容纳吸氢材料的氢分离器2。 版权所有(C)2009,JPO&INPIT
    • 7. 发明专利
    • Apparatus and method for control of powder
    • 用于控制粉末的装置和方法
    • JP2008200588A
    • 2008-09-04
    • JP2007038416
    • 2007-02-19
    • Toshiba Corp株式会社東芝
    • TAKASE HARUHIKOYAMADA KAZUYAKARASAWA TORU
    • B01J19/08B65B37/02
    • PROBLEM TO BE SOLVED: To enable avoiding troubles of powder apparatuses by phenomena including adhesion, coagulation and clogging effectively without adverse effects on the apparatuses.
      SOLUTION: An apparatus for controlling powder has ferromagnetic bodies 11 which are mixed with a powder 1 in a powder apparatus 2 and consist of a grain or a small ball containing a magnetic material and a magnet 12 which is arranged outside the powder apparatus 2 and applies a magnetic field to the ferromagnetic bodies 11. The behavior of the powder 1 is controlled by changing the position of the ferromagnetic bodies 11 in the powder 1 through adjustment of the field from the magnet 12.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:为了能够有效地避免粉末装置的麻烦,包括粘合,凝结和堵塞等现象,而对装置没有不利影响。 解决方案:用于控制粉末的设备具有铁粉体11,其与粉末装置2混合在粉末装置2中,并且由粉末装置2外部的包含磁性材料的颗粒或小球构成,并且包括磁体12 通过从磁体12调整磁场来改变粉末1中的铁磁体11的位置来控制粉末1的性能。(C )2008,JPO&INPIT
    • 8. 发明专利
    • Apparatus for and method of thermochemically producing hydrogen
    • 热化学生产装置和方法
    • JP2008137824A
    • 2008-06-19
    • JP2006323587
    • 2006-11-30
    • Toshiba Corp株式会社東芝
    • NAKAMURA HIDEKITAKAHASHI RIYOUTATAKASE HARUHIKOYAMADA KAZUYAMURAKAMI KAZUOJINBO NOBORU
    • C01B3/02
    • PROBLEM TO BE SOLVED: To improve the efficiency of hydrogen production by obtaining sulfur dioxide from hydrogen sulfide and sulfur generated as by-products in the reaction of hydrogen iodide with sulfuric acid and then applying a Bunsen reaction to the obtained sulfur dioxide together with iodine.
      SOLUTION: The objective apparatus for thermochemically producing hydrogen includes: a Bunsen reactor 3 in which iodine 14, sulfur dioxide 15 and water 11 are thermochemically decomposed to form hydrogen iodide 16 and sulfuric acid 17; an HI (hydrogen iodide) distiller 4 for separating the iodine 14 from the generated hydrogen iodide 16; an HI decomposer 5 for decomposing the iodine-separated hydrogen iodide 16 into hydrogen 12 and iodine 14; a sulfuric acid decomposer 1 for decomposing the generated sulfuric acid 17 into sulfur trioxide 22 and the water 11; a sulfur trioxide decomposer 2 for decomposing the sulfur trioxide 22 into sulfur dioxide 15 and oxygen 13; and an oxygen addition means 25 for adding the oxygen 13 to a phase comprising the sulfuric acid 17 as a main component to control them at a prescribed temperature.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:通过从硫化氢和硫化氢与硫酸的反应中产生的副产物硫化氢和硫获得二氧化硫,然后一起向所得二氧化硫施加本生反应,提高氢气生产的效率 用碘。 解决方案:用于热化学生产氢的目标装置包括:其中碘14,二氧化硫15和水11被热化学分解以形成碘化氢16和硫酸17的本生反应器3; 用于从产生的碘化氢16分离碘14的HI(碘化氢)蒸馏器4; 用于将碘分离的碘化氢16分解成氢12和碘14的HI分解器5; 用于将产生的硫酸17分解为三氧化硫22和水11的硫酸分解器1; 用于将三氧化硫22分解成二氧化硫15和氧13的三氧化硫分解器2; 以及氧气添加装置25,用于将氧气13加入到以硫酸17为主要成分的相中,以在规定温度下进行控制。 版权所有(C)2008,JPO&INPIT
    • 9. 发明专利
    • Method and apparatus for producing hydrogen iodide
    • 生产氢碘酸盐的方法和装置
    • JP2008024551A
    • 2008-02-07
    • JP2006199303
    • 2006-07-21
    • Toshiba Corp株式会社東芝
    • TAKAHASHI RIYOUTANAKAMURA HIDEKIJINBO NOBORUTAKASE HARUHIKOYAMADA KAZUYA
    • C01B7/13
    • PROBLEM TO BE SOLVED: To effectively isolate hydrogen iodide from the lower phase liquid containing hydrogen iodide obtained by the Bunsen reaction.
      SOLUTION: The method for producing hydrogen iodide contains a reaction process for forming hydrogen iodide and sulfuric acid by reacting sulfur dioxide, iodine and water, a separation process for separating hydrogen iodide and sulfuric acid respectively into two phases, viz. an upper phase liquid and a lower phase liquid, and a removal process for removing sulfur compounds from the lower phase liquid. The reaction process is implemented under a pressure condition of ≥0.1 MPa. Before the removal process, a separating liquid (e.g. an ionic liquid) having specific gravity between those of the upper phase liquid and the lower phase liquid and chemically stable against the upper phase liquid and the lower phase liquid is added.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:为了有效地从含有通过本生反应得到的碘化氢的液相中分离碘化氢。 解决方案:碘化氢的制造方法包括通过二氧化硫,碘和水反应形成碘化氢和硫酸的反应方法,分别将碘化氢和硫酸分离成两相的分离方法,即, 上相液和下相液,以及从下相液中除去硫化合物的去除方法。 反应过程在≥0.1MPa的压力条件下进行。 在去除过程之前,加入在上相液体和下相液体之间具有比重的分离液体(例如离子液体),并且对上相液体和下相液体具有化学稳定性。 版权所有(C)2008,JPO&INPIT
    • 10. 发明专利
    • Water purification sludge treatment apparatus and method
    • 水净化处理装置和方法
    • JP2007144366A
    • 2007-06-14
    • JP2005345990
    • 2005-11-30
    • Toshiba Corp株式会社東芝
    • OSAKI MASAHIKOYAMADA KAZUYASEKI HIDEJIYASUMURA KEIJIROFUNATSU TETSUYAASHIKI TATSUO
    • C02F11/18C02F1/52C02F11/00C02F11/12
    • PROBLEM TO BE SOLVED: To provide a water purification sludge treatment apparatus and method which can facilitate separation of sludge and water, and maintain an excellent quality of the separated water. SOLUTION: Raw water for drinking water is precipitated in a settling tank 1, and precipitated sludge is subjected to concentration treatment in a concentration tank 4. In the middle of transportation of concentrated sludge, the sludge during transportation is pressurized to a pressure equal to or higher than the atmospheric pressure and not more than 1 MPa by a pressurizing means 5, and heated to a heat treatment temperature of ≥100°C and ≤130°C by a heater 7. The temperature is held for 5 minutes or longer by a temperature holding part 8, and then cooled to a temperature suitable for dehydration treatment. The cooled sludge is returned to the atmospheric pressure by a pressure control part 12 to be dehydrated by a dehydrator 13. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种能够促进污泥和水分离的水净化污泥处理装置和方法,并且保持分离水的优良品质。

      解决方案:饮用水原水在沉淀池1中沉淀,沉淀污泥在浓缩池4中进行浓缩处理。在浓缩污泥运输过程中,运输过程中的污泥被加压至压力 通过加压装置5等于或高于大气压并且不大于1MPa,并通过加热器7加热至≥100℃和≤130℃的热处理温度。将温度保持5分钟或 通过温度保持部8更长,然后冷却至适于脱水处理的温度。 冷却的污泥通过压力控制部分12返回大气压,由脱水器13脱水。(C)2007,JPO&INPIT