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    • 1. 发明专利
    • Hydrogen producing apparatus and hydrogen producing method
    • 氢生产装置​​和氢生产方法
    • JP2006206334A
    • 2006-08-10
    • JP2005016206
    • 2005-01-25
    • Hitachi Ltd株式会社日立製作所
    • SASAHIRA AKIRAKARASAWA HIDETOSHIHOSHINO KUNIYOSHI
    • C01B3/06C01B3/02
    • Y02E60/36
    • PROBLEM TO BE SOLVED: To provide a hydrogen producing apparatus and a hydrogen producing method by which hydrogen can be efficiently produced regardless of the temperature of a heat source used in production of hydrogen. SOLUTION: The hydrogen producing apparatus 1a comprises: a high temperature gas furnace 2 (first heat source); a hydrogen production section where hydrogen is produced by accelerating the reduction reaction of water with sulfur dioxide by heat supplied from the high temperature gas furnace 2; and a sulfur trioxide decomposer 17 which reproduces sulfur dioxide by decomposing sulfur trioxide produced as a by-product by the reduction reaction in the hydrogen production section and which supplies the reproduced sulfur dioxide to the hydrogen production section, and further comprises an electric heater 17a which is a second heat source different from the high temperature gas furnace 2, wherein the sulfur trioxide decomposer 17 decomposes sulfur trioxide by heat supplied from the electric heater 17a. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供氢制造装置和氢制造方法,通过该方法可以有效地制造氢,而与用于制造氢的热源的温度无关。 解决方案:制氢装置1a包括:高温气体炉2(第一热源); 通过从高温气​​体炉2供给的热量加速二氧化硫的还原反应而产生氢的氢气生成部; 和三氧化硫分解器17,其通过在氢气产生部分中通过还原反应分解作为副产物产生的三氧化硫并且将再生的二氧化硫供应到氢气产生部分来再生二氧化硫,并且还包括电加热器17a,其中 是与高温气体炉2不同的第二热源,其中三氧化硫分解器17通过从电加热器17a供给的热分解三氧化硫。 版权所有(C)2006,JPO&NCIPI
    • 4. 发明专利
    • REPROCESSING METHOD FOR SPENT NUCLEAR FUEL
    • JPH11287890A
    • 1999-10-19
    • JP9122998
    • 1998-04-03
    • HITACHI LTD
    • KAMOSHITA MAMORUSASAHIRA AKIRAFUKAZAWA TETSUO
    • G21C19/46G21F9/06
    • PROBLEM TO BE SOLVED: To reprocess spent fast reactor fuel at low cost, by recovering plutonium and uranium from fast reactor fuel in a reprocessing facility for fast reactor and from light water reactor fuel and recovered residual liquid of facility for fast reactor. SOLUTION: Sheared pieces of fast reactor accepted in a reprocessing facility are heated and solved in nitric acid as solution, which is controlled at specific concentration of uranium, plutonium and nitric acid and sent to a multiple step extraction device. The solution is flown from the first step to the final step of the multiple step extractor. Also, mixture solvent of a specific composition is flown from the final step to the first step at a specific flow ratio. By this, the mixture in mixed oxide(MOX) fuel composition can be separated. The solution liquid from the final step of the multiple step extractor is sent to a reprocessing facility for light water reactor. On the other hand, mixed solvent which uranium and plutonium are extracted from is contacted in counter- current with diluted nitric acid water solution containing reducer by using the multiple step extractor. By this, the mixture of totally stripped plutonium and uranium is taken out as diluted nitric acid water solution, denitrated and converted into oxide to be MOX fuel.
    • 9. 发明专利
    • Hydrogen production system
    • 氢生产系统
    • JP2006282413A
    • 2006-10-19
    • JP2005100960
    • 2005-03-31
    • Hitachi Ltd株式会社日立製作所
    • SHIINA KOJIKARASAWA HIDETOSHISASAHIRA AKIRAHOSHINO KUNIYOSHI
    • C01B3/38G21D9/00
    • Y02P20/129
    • PROBLEM TO BE SOLVED: To provide a technology which is related to a hydrogen production system using waste heat from spent nuclear fuel in an atomic power station, which is particularly suitable for the effective utilization of energy and where temperature fitting to reaction conditions in hydrogen production can be suitably controlled. SOLUTION: The hydrogen production system (50) is equipped with a heat generator (1) to seal a nuclear waste releasing waste heat and a hydrogen producer (18) to produce hydrogen (F) using the waste heat as reaction heat and has an intermediate heat exchanger (10) where the waste heat is transferred for heating, a primary fluid (A) to transfer the waste heat by recycling it between the heat generator (1) and the intermediate heat exchanger (10) and a secondary fluid (B) to transfer the reaction heat by recycling it between the hydrogen producer (18) and the intermediate heat exchanger (10). COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种与在原子能发电站中使用来自乏核燃料的废热的氢气生产系统有关的技术,其特别适用于有效利用能量以及适合于反应条件的温度 在氢气生产中可以适当控制。 解决方案:氢气生产系统(50)装备有用于将废热排放废热和氢气生产器(18)的热发生器(1)用废热作为反应热产生氢气(F), 具有中间热交换器(10),其中废热被传送用于加热,主流体(A)通过在发热器(1)和中间热交换器(10)之间再循环来传递废热,并且辅助流体 (B)通过在氢气生产器(18)和中间热交换器(10)之间循环来传递反应热。 版权所有(C)2007,JPO&INPIT
    • 10. 发明专利
    • Method and device for reprocessing spent nuclear fuel
    • 代替核燃料燃料的方法和装置
    • JP2005195498A
    • 2005-07-21
    • JP2004003146
    • 2004-01-08
    • Hitachi Ltd株式会社日立製作所
    • HOSHINO KUNIYOSHISASAHIRA AKIRAKAWAMURA FUMIO
    • G21C19/44
    • Y02W30/882
    • PROBLEM TO BE SOLVED: To continuously perform a process for separating U and Pu from spent nuclear fuel. SOLUTION: Spent nuclear fuel and a fluorinating agent are continuously supplied to a flame-type reactor 2 so that the nuclear fuel is on the center side while the fluorinating agent is around the spent fuel. The amount of fluorinating agent supplied is controlled so as to be 1.3 to 1.5 times of an amount necessary for fluorination reaction of supplied spent nuclear fuel based on the amount of supplied spent nuclear fuel. The temperature of spent nuclear fuel may once be kept at 200 to 400°C (473 to 673°K), the nuclear fuel including uranium and plutonium after the fluorination reaction. COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:连续执行将U和Pu与废核燃料分离的处理。 解决方案:将耗费的核燃料和氟化剂连续地供应到火焰式反应器2,使得核燃料在中心侧,而氟化剂在废燃料周围。 将供给的氟化剂的量控制在供给的无用核燃料的氟化反应所需的量的1.3〜1.5倍。 废核燃料的温度可能一度保持在200〜400℃(473〜673°K),核燃料包括氟化反应后的铀和钚。 版权所有(C)2005,JPO&NCIPI