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1. 发明专利

JP2006161119A Vacuum carburizing apparatus and method therefor 有权
标题翻译：真空加湿装置及其方法
公开(公告)号：JP2006161119A
公开(公告)日：2006-06-22
申请号：JP2004356187
申请日：2004-12-09
申请人： Ishikawajima Harima Heavy Ind Co Ltd , 石川島播磨重工業株式会社
发明人： NAKABAYASHI TAKASHI , SHIGEGAKI YASUHIRO , NAKAI HIROSHI , TAKAHASHI JINICHIRO , TAKAHASHI KATSUMI
IPC分类号： C23C8/20 , C21D1/76 , F27B5/04 , F27B5/16 , F27B5/18
摘要： PROBLEM TO BE SOLVED: To provide a vacuum carburizing apparatus which can convert an easily available saturated hydrocarbons gas (such as town gas and propane gas) to a gas containing an unsaturated hydrocarbon such as acetylene or a hydrocarbon radical group, can stably supply a high concentration of or a wide concentration range of an acetylene-containing gas, and can reduce a gas that does not contribute or gives adverse effects to carburization in a furnace, and to provide a method therefor.
SOLUTION: This vacuum carburizing apparatus comprises a conversion unit 10 for converting the saturated hydrocarbon gas 1 to a converted gas 2 containing the unsaturated hydrocarbon such as acetylene or the hydrocarbon radical group, a gas-analyzing unit 12 for analyzing a gas composition of the converted gas, a vacuum carburizing furnace 14 which uses a carburizing gas 4 containing the unsaturated hydrocarbon such as acetylene or the hydrocarbon radical group, and a conversion control unit 16 for controlling the conversion unit, wherein the conversion control unit controls the concentration of the unsaturated hydrocarbon (such as acetylene and ethylene) contained in the carburizing gas 4 to a desired range.
COPYRIGHT: (C)2006,JPO&NCIPI
摘要翻译：要解决的问题：提供一种真空渗碳装置，其能够将容易获得的饱和烃气体（如城镇煤气和丙烷气体）转化为含有不饱和烃如乙炔或烃基团的气体，可以稳定地提供高浓度或较宽的含乙炔气体的浓度范围，并且可以减少对炉中的渗碳无贡献或不利影响的气体，并提供其方法。解决方案：该真空渗碳装置包括用于将饱和烃气体1转化成含有不饱和烃如乙炔或烃基团的转化气体2的转化单元10，用于分析气体组成的气体分析单元12 的转化气体的真空渗碳炉14，其使用含有不饱和烃如乙炔或烃基的渗碳气体4，以及用于控制转化单元的转化控制单元16，其中转化控制单元控制包含在渗碳气体4中的不饱和烃（例如乙炔和乙烯）达到所需范围。版权所有（C）2006，JPO＆NCIPI

2. 发明专利

JP2004096821A Method and apparatus for power generation 审中-公开
公开(公告)号：JP2004096821A
公开(公告)日：2004-03-25
申请号：JP2002251358
申请日：2002-08-29
申请人： Ishikawajima Harima Heavy Ind Co Ltd , 石川島播磨重工業株式会社
发明人： UCHIDA KUMIKO , NAKAI HIROSHI
IPC分类号： H01L35/30 , H01L35/00 , H01L35/34 , H02N6/00 , H02N11/00
摘要： PROBLEM TO BE SOLVED: To secure electric power at a site where there is no commercial power supply, and to improve portability of a generator.
SOLUTION: The generator comprises a thermoelectric conversion means 1 between a high-temperature heat source A and a low-temperature heat source B, and an external output means 8, which outputs the electric power generated by the thermoelectric conversion means 1 to the outside. The high-temperature heat source A is provided with a light-condensing body 6, that condenses sunlight X.
COPYRIGHT: (C)2004,JPO

3. 发明专利

JP2005040654A Method for manufacturing nox decomposing catalyst 有权
标题翻译：制备NOX分解催化剂的方法
公开(公告)号：JP2005040654A
公开(公告)日：2005-02-17
申请号：JP2003200002
申请日：2003-07-22
申请人： Ishikawajima Harima Heavy Ind Co Ltd , 石川島播磨重工業株式会社
发明人： UCHIDA KUMIKO , NAKAI HIROSHI , AYABE TSUNEO , TSUBOUCHI NOBUICHI
IPC分类号： B09B3/00 , B01D53/94 , B01J23/22 , B01J37/03 , B01J37/06 , B01J37/30 , C02F11/00
摘要： PROBLEM TO BE SOLVED: To provide a method for manufacturing a NOx decomposing catalyst from waste containing Ti, V and Al. SOLUTION: This method comprises a step to prepare an acid-dissolved liquid 13 by dissolving a starting material 11 composed of the waste containing Ti, V and Al in an acidic solution 12, a step to produce a precipitate 15 by adding an alkaline solution 14 to the acid-dissolved liquid 13, a step A to purify the precipitate 15, a step to withdraw a mixture of titanium hydroxide and vanadium hydroxide as a catalyst precursor 16 and a step B to fire the precursor 16 at 300-600°C, so that the NOx decomposing catalyst 17 being a fired material of titanium hydroxide and vanadium hydroxide is manufactured. COPYRIGHT: (C)2005,JPO&NCIPI
摘要翻译：解决的问题：提供一种由含有Ti，V和Al的废物制造NOx分解催化剂的方法。解决方案：该方法包括通过将由含有Ti，V和Al的废物构成的起始材料11溶解在酸性溶液12中来制备酸溶液13的步骤，通过加入碱溶液14加入到酸溶液13中，纯化沉淀物15的步骤A，取出氢氧化钛和作为催化剂前体16的氢氧化钒和步骤B的混合物的步骤，以300-600 ℃，从而制造作为氢氧化钛和氢氧化钒的烧成物的NOx分解催化剂17。版权所有（C）2005，JPO＆NCIPI

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