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    • 1. 发明授权
    • Magnetic separation filtering and cleaning apparatus
    • 磁选过滤和清洗装置
    • US08002976B2
    • 2011-08-23
    • US12019674
    • 2008-01-25
    • Norihide SahoHisashi IsogamiAkira MochizukiTomoko Akiyama
    • Norihide SahoHisashi IsogamiAkira MochizukiTomoko Akiyama
    • B01D35/06B03C1/30C02F1/48
    • B03C1/12B03C1/30B03C2201/18C02F1/001C02F1/44C02F1/488C02F1/5236C02F1/56C02F1/66C02F2209/42
    • A magnetic separation filtering and cleaning apparatus for adding flocculant and magnetic powder to raw water containing pollutant particles to form magnetic floc in treated fluid and separating and removing the magnetic floc from the treated fluid, comprising: a magnetic field generation device being provided in a rotating body for suctioning the magnetic floc on a surface of the rotating body from the treated fluid containing the magnetic floc, a magnetic field rotating device for rotating the magnetic field generation device, a sludge recovery device for separating sludge including the magnetic floc mechanically from the surface of the rotating body of the magnetic field generation device; and a filtering device having a rotating net for filtering out the magnetic floc from the treated fluid including the magnetic floc and flowing down the treated fluid filtered through the rotating net.
    • 一种磁选分离过滤和清洗装置,用于将絮凝剂和磁粉加入含污染物颗粒的原水中以在处理过的流体中形成磁絮凝物,并从处理过的流体中分离和除去磁絮凝物,其特征在于包括:磁场产生装置, 用于从包含磁絮状物的处理液体旋转体的表面吸附磁絮体的主体,用于旋转磁场产生装置的磁场旋转装置,用于将包含磁絮凝物的污泥与表面机械分离的污泥回收装置 的磁场产生装置的旋转体; 以及过滤装置,其具有旋转网,用于从包括磁絮凝物的处理过的流体过滤掉磁絮凝物并向下流过经过旋转网过滤的处理过的流体。
    • 3. 发明申请
    • METHOD AND DEVICE FOR REMOVING CO2 AND H2S
    • 用于去除CO2和H2S的方法和装置
    • US20100101416A1
    • 2010-04-29
    • US12581725
    • 2009-10-19
    • Tomoko Akiyama
    • Tomoko Akiyama
    • B01D53/14B01D53/18
    • B01D53/1406B01D53/02B01D53/1425B01D53/1462B01D2251/102B01D2253/112B01D2255/20707B01D2255/20769B01D2256/24B01D2257/302B01D2259/80C01B17/0408C01B17/167C10L3/10C10L3/102Y02C10/04Y02C10/06Y02P20/152
    • A method and a device for removing acidic materials, such as CO2 and H2S, with limited energy consumption are provided. The method comprises a step of introducing the feed gas into a first absorber, and removing CO2 and H2S from the feed gas by contacting the feed gas with a lean solution in the first absorber; and a step of introducing the feed gas into a second absorber, and removing CO2 and H2S remaining in the feed gas by contacting the feed gas with a semi-lean solution in the second absorber. The rich solution having absorbed CO2 and H2S in the first and second absorber is introduced into a flash drum where an internal pressure is kept lower than that in the first absorber and in the second absorber. After a part of CO2 and H2S is released from the rich solution in the flash drum to obtain a semi-lean solution, a part of the semi-lean solution is cooled and introduced into the second absorber to contact with the feed gas in the second absorber. A remaining part of the semi-lean solution is introduced into a stripper and heated to release remaining CO2 and H25 from the semi-lean solution and to obtain a lean solution. A part of the lean solution is cooled and introduced into the first absorber to contact with the feed gas in the first absorber. A remaining part of the lean solution is cooled, introduced into the second absorber at an upper level of the second absorber, and is contacted with the feed gas in the second absorber, and thereby obtaining a treated gas.
    • 提供了一种用于去除酸性物质如CO 2和H 2 S的方法和装置,其能量有限。 该方法包括将进料气体引入第一吸收器中,并且通过使进料气体与第一吸收器中的贫溶液接触,从进料气体中除去CO 2和H 2 S. 以及将进料气体引入第二吸收器的步骤,以及通过使进料气体与第二吸收器中的半贫溶液接触来除去剩余在进料气体中的CO 2和H 2 S. 在第一和第二吸收器中吸收CO 2和H 2 S的富溶液被引入闪蒸鼓中,其中内压保持低于第一吸收器和第二吸收器中的内压。 在一部分二氧化碳和硫化氢从闪蒸罐中的富溶液中释放以获得半贫溶液后,将半贫溶液的一部分冷却并引入第二吸收器以与第二吸收器中的进料气体接触 吸收器。 将半贫溶液的剩余部分引入汽提器中并加热以从半贫溶液中释放剩余的CO 2和H 25并获得贫溶液。 将贫溶液的一部分冷却并引入第一吸收器中以与第一吸收器中的进料气体接触。 将贫溶液的剩余部分冷却,在第二吸收器的上层引入第二吸收器,并与第二吸收器中的进料气体接触,从而获得处理气体。