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    • 1. 发明专利
    • Apparatus for directly cracking lower hydrocarbon
    • 直接破碎下层油料的装置
    • JP2006096590A
    • 2006-04-13
    • JP2004282763
    • 2004-09-28
    • Japan Steel Works Ltd:TheKajima CorpAsao Tada旭男 多田株式会社日本製鋼所鹿島建設株式会社
    • TADA ASAOTOGO YOSHITAKATAKASAGO HIROYUKINAKAMURA SATOSHIITO HIDEAKI
    • C01B3/26B01J23/94B01J38/00C01B3/02
    • Y02P20/584
    • PROBLEM TO BE SOLVED: To provide an apparatus for directly cracking lower hydrocarbons capable of continuously removing hydrogen and solid carbon. SOLUTION: A heat resistant coil-shaped reaction tube 2 is heated by a heating means 10 to a cracking reaction temperature. A lower hydrocarbon gas M (for example, methane gas) and a catalyst powder T for direct cracking reaction of the hydrocarbon are concurrently delivered from a delivery apparatus 20 to one end 3 of the reaction tube 2. A generated cracking gas (for example, hydrogen) and the catalyst powder T discharged from the other end 5 of the reaction tube 2 are separated in a separating apparatus 30. The delivery apparatus 20 comprises a blower 21 for injecting the lower hydrocarbon gas flow M and a catalyst charging device 22 for mixing the catalyst powder T into the gas flow M from the blower 21. The catalyst powder T separated in the separating apparatus 30 is returned back to the catalyst charging device 22. The separating apparatus 30 comprises an unreacted gas-separating apparatus 34 for separating the generated cracking gas from the unreacted low hydrocarbon gas M. The unreacted gas M separated in the unreacted gas-separating apparatus 34 is returned back to the blower 21 or to the gas flow M. The heating means 10 is mounted so that it is aligned with the central axis of the coil-shaped reaction tube 2. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种用于直接裂解能够连续除去氢和固体碳的低级烃的装置。 解决方案:将耐热线圈形反应管2通过加热装置10加热到裂化反应温度。 烃的直接裂解反应的低级烃气体M(例如甲烷气体)和催化剂粉末T从输送装置20同时输送到反应管2的一端。产生的裂解气体(例如, 氢),从反应管2的另一端5排出的催化剂粉末T在分离装置30中分离。输送装置20包括用于喷射下部烃类气体流M的鼓风机21和用于混合的催化剂填充装置22 催化剂粉末T进入来自鼓风机21的气流M.在分离装置30中分离的催化剂粉末T返回到催化剂装料装置22.分离装置30包括未反应气体分离装置34,用于将产生的 从未反应的低碳氢化合物气体M中裂解气体。未反应气体分离装置34中分离的未反应气体M返回到鼓风机21或气流 加热装置10安装成使其与线圈形反应管2的中心轴线对准。版权所有(C)2006,JPO&NCIPI
    • 4. 发明专利
    • Method for manufacturing hydrogen occlusion alloy
    • 制造氢化合金的方法
    • JP2007084883A
    • 2007-04-05
    • JP2005275687
    • 2005-09-22
    • Japan Steel Works Ltd:The株式会社日本製鋼所
    • KUBO KAZUYAKABUTOMORI TOSHIKIONUKI SOUMEIARASHIMA HIRONOBUHASHI KUNIHIKOITO HIDEAKI
    • C22F1/18B22F1/00B22F9/04C22C1/00C22C30/00C22F1/00H01M4/38H01M8/04
    • H01M4/383B22F9/04B22F2998/10C22C1/00C22C1/0491C22C30/00C22F1/18H01M8/04216H01M8/065B22F9/06B22F1/0085B22F9/023
    • PROBLEM TO BE SOLVED: To provide a hydrogen occlusion alloy with which the hydrogen can effectively be absorbed and discharged, and excellent occlusion quantity of the hydrogen and effective moving quantity of the hydrogen are shown and further, excellent durability is shown. SOLUTION: To the powdery hydrogen occlusion alloy, a strain-removal annealing for heating at 600-1200°C for 10min to 30 hr is performed. It is desirable that the grain size of the hydrogen occlusion alloy powder is made to be ≤10μm, and this hydrogen occlusion alloy is BCC phase (body-centered cubic structure) as the main phase. Since the strain at the initial stage before hydrogenating, is removed, the hydrogen solid-solution range is drastically decreased and the hydrogen occlusion quantity at the initial stage and the effective hydrogen moving quantity are increased. Storing and spreading of the strain are drastically reduced by making into the powder and the development of the strain at the storing time of the hydrogen is drastically reduced, and the drastic increasing effect of an absorbing plateau property is obtained and further, the deteriorating ratio caused by repeating of the storing and the discharging of the hydrogen is drastically improved. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了提供可以有效地吸收和排出氢的氢吸收合金,并且显示了优异的氢吸留量和氢的有效移动量,此外,显示出优异的耐久性。 解决方案:对于粉末状的吸氢合金,进行在600-1200℃下加热10分钟至30小时的除菌退火。 优选使吸氢合金粉末的粒径≤10μm,该吸氢合金为BCC相(体心立方结构)为主相。 由于在氢化之前的初始阶段的应变被去除,所以氢固溶体范围急剧下降,初始阶段的吸氢量和有效氢的移动量增加。 通过制成粉末而使应变的储存和铺展显着降低,并且在氢的储存时间下菌株的发展急剧减少,并且获得了吸收平台性能的急剧增加的效果,而且, 通过重复氢气的储存和排放,显着提高。 版权所有(C)2007,JPO&INPIT
    • 5. 发明专利
    • Catalyst for direct decomposition of lower hydrocarbon
    • 催化剂用于低碳氢化合物的直接分解
    • JP2006043645A
    • 2006-02-16
    • JP2004231736
    • 2004-08-06
    • Japan Steel Works Ltd:TheKajima CorpAsao Tada旭男 多田株式会社日本製鋼所鹿島建設株式会社
    • TADA ASAOTOGO YOSHITAKATAKASAGO HIROYUKINAKAMURA SATOSHIITO HIDEAKI
    • B01J23/745C01B3/26C01B31/02H01M8/06
    • Y02E60/50
    • PROBLEM TO BE SOLVED: To provide a catalyst for direct decomposition of lower hydrocarbon which is friendly to environment and is economical. SOLUTION: The catalyst for direct decomposition of lower hydrocarbon is prepared by depositing iron on a surface of a carrier consisting essentially of silica (SiO 2 ) via covering of non-ferrous metal oxide. For example, after the carrier consisting essentially of silica is impregnated with a non-ferrous metal salt solution and then is dried and calcined, the carrier is impregnated with the mixed solution of the non-ferrous metal salt and an iron salt and then is dried and calcined. Preferably the non-ferrous metal oxide is alumina (Al 2 O 3 ). More preferably foamed glass is used as the carrier consisting essentially of silica. The foamed glass can be obtained as a bulk phase porous body, for example, by adding a foaming agent to pulverized matter of waste glass and performing melting and foaming. The foamed glass having higher ratio of continuous air pores compared to closed cells is desirable. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种直接分解对环境友好且经济的低级烃的催化剂。 解决方案:通过覆盖有色金属氧化物,通过在基本上由二氧化硅(SiO 2 SB 2)组成的载体的表面上沉积铁来制备用于直接分解低级烃的催化剂。 例如,在基本上由二氧化硅组成的载体用非铁金属盐溶液浸渍之后,将其干燥和煅烧,用非铁金属盐和铁盐的混合溶液浸渍载体,然后干燥 并煅烧。 优选地,有色金属氧化物是氧化铝(Al 2 SB 3 O 3 / SB 3)。 更优选使用泡沫玻璃作为主要由二氧化硅组成的载体。 作为体相多孔体,例如可以通过在废玻璃的粉碎物中添加发泡剂,进行熔融发泡而得到发泡玻璃。 与闭孔相比,具有较高连续空气孔率的泡沫玻璃是理想的。 版权所有(C)2006,JPO&NCIPI
    • 10. 发明专利
    • Method for removing solvent from solvated hydrogen storage material
    • 从溶解氢储存材料中除去溶剂的方法
    • JP2009249258A
    • 2009-10-29
    • JP2008101512
    • 2008-04-09
    • Japan Steel Works Ltd:TheTohoku Univ国立大学法人東北大学株式会社日本製鋼所
    • NAKAMORI HIROKOIKEDA KAZUTAKAORIMO SHINICHIHASHI KUNIHIKOITO HIDEAKIKABUTOMORI TOSHIKI
    • C01B6/06B01J20/02
    • PROBLEM TO BE SOLVED: To efficiently remove a solvent from a solvated hydrogen storage material without causing release of hydrogen.
      SOLUTION: A solvent such as ether is removed from a solvate of a hydrogen storage material, such as AlH
      3 -ether solvate, by heating the solvate of the hydrogen storage material with microwaves preferably so that the hydrogen storage material is not heated to a temperature not lower than the temperature at which the hydrogen storage material releases hydrogen. Since the microwaves directly act on solvent molecules, the solvated solvent is eliminated, the desolvated hydrogen storage material does not absorb microwaves, and the microwaves pass through the desolvated hydrogen storage material. Thereby, the microwaves reach the inside of the desolvated hydrogen storage material to perform a desolvation treatment of a large amount of material in a short time.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:有效地从溶剂化的储氢材料中除去溶剂而不会导致氢的释放。 解决方案:通过用微波加热储氢材料的溶剂化物,从诸如AlH 3 S 3 - 醚溶剂合物的储氢材料的溶剂化物中除去溶剂如乙醚,优选使得 储氢材料不被加热到不低于储氢材料释放氢的温度的温度。 由于微波直接作用于溶剂分子,所以溶剂化溶剂被消除,脱溶剂的储氢材料不吸收微波,微波通过去溶的储氢材料。 由此,微波到达脱溶性储氢材料的内部,能够在短时间内进行大量材料的去溶剂化处理。 版权所有(C)2010,JPO&INPIT