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    • 1. 发明专利
    • Separation and regeneration apparatus of absorbing liquid and liquid carbon dioxide, and gas refining apparatus using the separation and regeneration apparatus
    • 吸收液体和二氧化碳的分离和再生装置以及使用分离装置和再生装置的气体精炼装置
    • JP2008178764A
    • 2008-08-07
    • JP2007012395
    • 2007-01-23
    • Mitsubishi Materials Corp三菱マテリアル株式会社
    • DEN TAKEYOSHIWANG JUNZHUTAI BUNHINMORI RYOHEIKOIZUMI HIROMICHIIIMURA TAKESHI
    • B01D53/14B01D17/00B01D17/025B01D17/04B01J19/00C01B3/38C01B32/50H01M8/06
    • Y02A50/2342Y02C10/06Y02P20/152
    • PROBLEM TO BE SOLVED: To provide a separation and regeneration apparatus in which a phase separation efficiency of an absorbing liquid and liquid carbon dioxide is prevented from being degraded. SOLUTION: The absorbing liquid 11 having absorbed carbon dioxide gas is cooled in a cooler 26 to be an absorbing liquid dispersed with free liquid droplets of liquid carbon dioxide 13. The separation and regeneration apparatus 23 separates liquid carbon dioxide from the absorbing liquid cooled in the cooler and regenerates the absorbing liquid. A buffer tank 27 connected to an upper part of the separation and regeneration apparatus evaporates part of or all of the liquid carbon dioxide separated in the separation and regeneration apparatus and sent to the tank. A separation plate 23a vertically extendedly provided in the separation and regeneration apparatus demarcates the separation and regeneration apparatus into a separation chamber 23b and a settling chamber 23c. An upper communication hole 23d and a lower communication hole 23e formed in the separation plate communicate the separation chamber and settling chamber at an upper part and a lower part, respectively. A separation promoting part 23f provided at a center of the separation chamber collects, coagulates, and agglomerates the free liquid droplets of liquid carbon dioxide dispersed in the absorbing liquid. COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种分离和再生装置,其中防止吸收液体和液体二氧化碳的相分离效率降低。 吸收二氧化碳气体的吸收液11在冷却器26中被冷却,成为分散有液态二氧化碳13的自由液滴的吸收液。分离再生装置23将液体二氧化碳与吸收液分离 在冷却器中冷却并再生吸收液体。 与分离再生装置的上部连接的缓冲罐27将在分离再生装置中分离出的一部分或全部液体二氧化碳蒸发并送入罐中。 垂直延伸设置在分离和再生装置中的分隔板23a将分离和再生装置划分成分离室23b和沉降室23c。 形成在分隔板上的上连通孔23d和下连通孔23e分别在上部和下部连通分离室和沉降室。 设置在分离室的中心的分离促进部23f对分散在吸收液中的液态二氧化碳的游离液滴收集,凝结和附聚。 版权所有(C)2008,JPO&INPIT
    • 2. 发明专利
    • Washing method and washing apparatus
    • 洗衣方法和洗衣设备
    • JP2006247563A
    • 2006-09-21
    • JP2005069423
    • 2005-03-11
    • Mitsubishi Materials Corp三菱マテリアル株式会社
    • YAMANO YUURIKEIDEN TAKEYOSHIHATAKEYAMA KO
    • B08B7/00H01L21/304
    • PROBLEM TO BE SOLVED: To provide a washing apparatus made compact and easy to control and a washing method capable of efficiently removing impurities adhering to a part of an object member to be washed such as surface easy to be washed.
      SOLUTION: The washing method involves a first washing step of supplying a liquid washing solvent to a washing tank (1) housing an object member to be washed and bringing the liquid washing solvent into contact with the object member to be washed (W) and a second washing step of making the liquid washing solvent supplied to the washing tank be a supercritical fluid by heating in closed state and bringing the supercritical fluid into contact with the object member to be washed. The washing apparatus for the method is provided with a liquid cylinder (2) installed at a position higher than the washing tank and heating means (4) installed in the outer circumferential part or the inside of the washing tank (1) having means for bringing the object member to be washed into contact with the washing solvent for heating the liquid washing solvent and making the solvent be the supercritical fluid.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种紧凑且易于控制的洗涤装置以及能够有效地除去附着在待清洗对象部件的一部分上的杂质的洗涤方法,例如易于清洗的表面。 解决方案:洗涤方法包括:第一洗涤步骤,将洗涤溶剂供应到容纳待洗涤物体的洗涤槽(1),并使液体洗涤溶剂与待洗涤物体(W ),通过在关闭状态下加热使超临界流体与待洗涤物体接触的方式使供给洗涤槽的液体洗涤溶剂成为超临界流体的第二洗涤步骤。 该方法的洗涤装置设置有安装在比洗涤槽高的位置的液筒(2),并且安装在洗涤槽(1)的外周部分或内部的加热装置(4)具有用于 要洗涤的物体与洗涤溶剂接触以加热液体洗涤溶剂并使溶剂成为超临界流体。 版权所有(C)2006,JPO&NCIPI
    • 3. 发明专利
    • Method for imparting function to polymer substrate
    • 将功能转移到聚合物基板的方法
    • JP2006002009A
    • 2006-01-05
    • JP2004178663
    • 2004-06-16
    • Mitsubishi Materials Corp三菱マテリアル株式会社
    • DEN TAKEYOSHISAIKI WATARUHATAKEYAMA KOYAMANO YUURIKEISHINOHARA KATSUNORI
    • C08J7/02C08L101/00
    • Y02P20/544
    • PROBLEM TO BE SOLVED: To provide a method for imparting function to a polymer substrate, which controls surface precipitation of a functional additive from a fluid occurring on pressure reduction and removal of the functional additive injected to the substrate after function imparting.
      SOLUTION: The improved method for imparting function to a polymer substrate by supplying a supercritical fluid having dissolved a functional additive to a pressure container storing a polymer substrate comprises further a process for introducing liquid carbon dioxide to the pressure container, replacing the supercritical liquid having dissolved the functional additive in the pressure container with the liquid carbon dioxide and reducing pressure in the pressure container, into which the liquid carbon dioxide is introduced, to atmospheric pressure as an aftertreatment process after imparting function to the polymer substrate.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种赋予聚合物基材功能的方法,该方法控制功能添加剂在功能赋予后注入到基材上的压力降低和除去功能添加剂后发生的流体的表面沉淀。 解决方案:通过将具有溶解功能添加剂的超临界流体供给到储存聚合物基材的压力容器中来赋予聚合物基材的功能的改进方法还包括将液体二氧化碳引入压力容器的方法,代替超临界 将具有液体二氧化碳的功能添加剂溶解在压力容器中的液体,并且将引入液态二氧化碳的压力容器中的还原压力作为后处理工序赋予聚合物基材后的液体。 版权所有(C)2006,JPO&NCIPI
    • 10. 发明专利
    • Method for purifying contaminated soil using supercritical co2
    • 使用超临界二氧化碳净化污染土壤的方法
    • JP2007117944A
    • 2007-05-17
    • JP2005316512
    • 2005-10-31
    • Mitsubishi Materials CorpPetroleum Energy Center三菱マテリアル株式会社財団法人石油産業活性化センター
    • HATAKEYAMA KOOTA KAZUAKIRINAT MIRVARIEVDEN TAKEYOSHI
    • B09C1/02B01D11/00B09C1/08
    • PROBLEM TO BE SOLVED: To provide a method for purifying contaminated soil using supercritical CO 2 comprising efficiently purifying soil contaminated with petroleum products of light components such as gasoline, kerosene and light oil, and heavy components such as A-heavy oil and C-heavy oil, and the like, using supercritical CO 2 . SOLUTION: The method for purifying contaminated soil using supercritical CO 2 comprises: circulating liquid CO 2 supplied into a precirculation path 16 while controlling at a first temperature and a first pressure to convert the liquid CO 2 into supercritical CO 2 ; extracting a light component and a heavy component from soil to be treated contained in a cleaning tank 12; supplying the supercritical CO 2 into a separating-cooling tank 26 and cooling the supercritical CO 2 to decrease solubility and vapor pressure of the heavy component to the supercritical CO 2 and thereby separating the heavy component from the supercritical CO 2 ; heating the separated supercritical CO 2 by second temperature adjustment means 23 while dissolving the light component as an auxiliary solvent of the heavy component to be converted into a supercritical CO 2 and then circulating the supercritical CO 2 through a first circulation path 24 to remove the heavy component remaining in the soil to be treated; supplying the supercritical CO 2 into a separating-depressurizing tank 34 to be depressurized and converting the depressurized supercritical CO 2 into a CO 2 gas state to separate the light component from the CO 2 gas; and cooling the separated CO 2 gas to be converted into liquid CO 2 and then circulating the liquid CO 2 through a second circulation path 33 while heating and pressurizing to remove the light component remaining in the soil to be treated. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种使用超临界CO 2 SBS 2 净化污染土壤的方法,其包括有效地净化被汽油,煤油和轻油等轻质成分的石油产品污染的土壤和重质成分 如重油和C型重油等,使用超临界CO 2 。 解决方案:使用超临界CO 2 净化污染土壤的方法包括:在第一温度和第一温度下进行控制时供应到预循环路径16中的循环液体CO 2 将液体CO 2 转化为超临界CO 2 的压力; 从容纳在清洗槽12中的待处理土壤中提取轻质成分和重质成分; 将超临界CO 2 供应到分离冷却罐26中并冷却超临界CO SB> 2以降低重组分对超临界CO 2 SB 2的溶解度和蒸气压 从而将重组分与超临界CO 2 分离; 同时将作为重组分的辅助溶剂的轻组分溶解在待转化的超临界CO 2 SBB中,然后循环的同时,通过第二温度调节装置23加热分离的超临界CO 2 通过第一循环路径24超临界CO 2 以除去残留在待处理土壤中的重组分; 将超临界CO 2 供给到分离减压槽34中以进行减压,并将减压的超临界CO 2 SBS 2 转化为CO 2 气态, 将光组分与CO 2 气分离; 并将分离出的CO 2 SB 2气体冷却,以转化成液体CO 2 ,然后使液体CO 2 循环通过第二循环路径33,同时加热 并加压以除去留在待处理土壤中的光成分。 版权所有(C)2007,JPO&INPIT