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    Humidity control system
    1.
    发明授权
    Humidity control system 有权
    湿度控制系统

    公开(公告)号：US07874174B2

    公开(公告)日：2011-01-25

    申请号：US11887248

    申请日：2006-03-20

    申请人： Tomohiro Yabu ,  Eisaku Okubo

    发明人： Tomohiro Yabu ,  Eisaku Okubo

    IPC分类号： F25B23/00

    CPC分类号： F24F3/1411 ,  F24F3/1423 ,  F24F3/1429 ,  F24F2203/1032 ,  F24F2203/104 ,  F24F2203/1068 ,  F24F2203/1088 ,  F25B13/00 ,  F25B2313/02743

    摘要： A humidity control system during humidification operation sequentially repeats a first mode in which a second adsorption heat exchanger (82) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators, a second mode in which a third adsorption heat exchanger (83) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators and a third mode in which a first adsorption heat exchanger (81) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators. For example, during the first mode, the first adsorption heat exchanger (81) serving as an evaporator adsorbs moisture in a first air. Furthermore, in the second adsorption heat exchanger (82) serving as a condenser, the adsorbent is regenerated to humidify a second air. Furthermore, in the third adsorption heat exchanger (83) serving as an evaporator, the second air given moisture and heat in the second adsorption heat exchanger (82) is cooled. The humidity control system supplies the second air humidified by the second adsorption heat exchanger (82) and cooled by the third adsorption heat exchanger (83) to a room.

    摘要翻译： 加湿运转中的湿度控制系统依次重复第一模式，其中第二吸附热交换器（82）用作蒸发器，剩余的吸附热交换器用作蒸发器;第二模式，其中第三吸附热交换器（83） 作为蒸发器，剩余的吸附热交换器用作蒸发器，第三模式中第一吸附热交换器（81）用作蒸发器，剩余的吸附热交换器用作蒸发器。 例如，在第一模式中，用作蒸发器的第一吸附热交换器（81）吸收第一空气中的水分。 此外，在用作冷凝器的第二吸附热交换器（82）中，再生吸附剂以加湿第二空气。 此外，在用作蒸发器的第三吸附热交换器（83）中，在第二吸附热交换器（82）中给予湿气和热量的第二空气被冷却。 湿度调节系统供给由第二吸附热交换器（82）加湿并被第三吸附热交换器（83）冷却的室内的第二空气。

    Humidity Control System
    2.
    发明申请
    Humidity Control System 有权
    湿度控制系统

    公开(公告)号：US20090288444A1

    公开(公告)日：2009-11-26

    申请号：US11887248

    申请日：2006-03-20

    申请人： Tomohiro Yabu ,  Eisaku Okubo

    发明人： Tomohiro Yabu ,  Eisaku Okubo

    IPC分类号： F25B17/00

    CPC分类号： F24F3/1411 ,  F24F3/1423 ,  F24F3/1429 ,  F24F2203/1032 ,  F24F2203/104 ,  F24F2203/1068 ,  F24F2203/1088 ,  F25B13/00 ,  F25B2313/02743

    摘要： A humidity control system during humidification operation sequentially repeats a first mode in which a second adsorption heat exchanger (82) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators, a second mode in which a third adsorption heat exchanger (83) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators and a third mode in which a first adsorption heat exchanger (81) serves as an evaporator and the remaining adsorption heat exchangers serve as evaporators. For example, during the first mode, the first adsorption heat exchanger (81) serving as an evaporator adsorbs moisture in a first air. Furthermore, in the second adsorption heat exchanger (82) serving as a condenser, the adsorbent is regenerated to humidify a second air. Furthermore, in the third adsorption heat exchanger (83) serving as an evaporator, the second air given moisture and heat in the second adsorption heat exchanger (82) is cooled. The humidity control system supplies the second air humidified by the second adsorption heat exchanger (82) and cooled by the third adsorption heat exchanger (83) to a room.

    摘要翻译： 加湿运转中的湿度控制系统依次重复第一模式，其中第二吸附热交换器（82）用作蒸发器，剩余的吸附热交换器用作蒸发器;第二模式，其中第三吸附热交换器（83） 作为蒸发器，剩余的吸附热交换器用作蒸发器，第三模式中第一吸附热交换器（81）用作蒸发器，剩余的吸附热交换器用作蒸发器。 例如，在第一模式中，用作蒸发器的第一吸附热交换器（81）吸收第一空气中的水分。 此外，在用作冷凝器的第二吸附热交换器（82）中，再生吸附剂以加湿第二空气。 此外，在用作蒸发器的第三吸附热交换器（83）中，在第二吸附热交换器（82）中给予湿气和热量的第二空气被冷却。 湿度调节系统供给由第二吸附热交换器（82）加湿并被第三吸附热交换器（83）冷却的室内的第二空气。

    Partial oxidation reformer
    4.
    发明授权
    Partial oxidation reformer 失效
    部分氧化重整器

    公开(公告)号：US06770106B1

    公开(公告)日：2004-08-03

    申请号：US09914377

    申请日：2001-08-28

    申请人： Yasunori Okamoto ,  Nobuki Matsui ,  Shuji Ikegami ,  Kazuo Yonemoto ,  Eisaku Okubo ,  Isao Ohgami

    发明人： Yasunori Okamoto ,  Nobuki Matsui ,  Shuji Ikegami ,  Kazuo Yonemoto ,  Eisaku Okubo ,  Isao Ohgami

    IPC分类号： C01B338

    CPC分类号： C01B3/386 ,  B01J8/0242 ,  B01J8/025 ,  B01J8/0257 ,  B01J8/0446 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/1923 ,  B01J2219/1943 ,  C01B3/38 ,  C01B3/382 ,  C01B2203/0261 ,  C01B2203/066 ,  C01B2203/0805 ,  C01B2203/0811 ,  C01B2203/0816 ,  C01B2203/0844 ,  C01B2203/085 ,  C01B2203/1023 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1223 ,  C01B2203/1241 ,  C01B2203/1276 ,  C01B2203/1604 ,  C01B2203/80 ,  H01M8/0631

    摘要： Hydrogen-rich reformed gas is produced by reaction including partial oxidation of feed gas in a reforming reaction section (6). In this case, for the purpose of reducing temperature variations in the reforming reaction section (6), improving the thermal efficiency thereof and providing a reformer (A) with a simple and compact construction, the reformer (A) is formed in a double-wall structure consisting of a housing (1) and partitions (2), (2) inside of the housing (1), the reforming reaction section (6) is contained between the partitions (2), (2), and a feed gas passage (3) is provided by the space between the housing (1) and the partition (2). In this manner, the feed gas passage (3) is provided in the surrounding area of the reforming reaction section (6). The reforming reaction section (6) is thermally insulated by the feed gas passage (3) so that temperature variations in the reforming reaction section (6) can be reduced. The feed gas in the feed gas passage (3) is preheated by heat of reaction in the reforming reaction section (6) so that the self-recovery of heat can improve thermal efficiency of the reformer (A). In addition, a preheater for preheating the feed gas can be formed integrally between the feed gas passage (3) and the reforming reaction section (6) thereby compacting the construction of the reformer.

    摘要翻译： 通过在重整反应部分（6）中进料气体的部分氧化反应产生富氢重整气体。 在这种情况下，为了降低重整反应部（6）的温度变化，提高其热效率，提供简单紧凑的结构的重整器（A），重整器（A） （2），壳体（1）内部的隔板（2），（2）构成的壁结构，重整反应部分（6）被容纳在隔板（2），（2）之间， 通道（3）由壳体（1）和隔板（2）之间的空间提供。 以这种方式，在重整反应部（6）的周围区域设置有进料气体通路（3）。 重整反应部（6）通过进料气体通路（3）进行绝热，能够降低重整反应部（6）的温度变化。 进料气体通道（3）中的进料气体通过重整反应段（6）中的反应热被预热，使得热回收能够提高重整器（A）的热效率。 此外，用于预热进料气体的预热器可以一体地形成在进料气体通道（3）和重整反应部分（6）之间，从而压实重整器的结构。

    Plate type heat exchanger
    6.
    发明授权
    Plate type heat exchanger 失效
    板式换热器

    公开(公告)号：US06394178B1

    公开(公告)日：2002-05-28

    申请号：US09622060

    申请日：2000-08-25

    申请人： Kaori Yoshida ,  Takeshi Ebisu ,  Eisaku Okubo ,  Katsuhiko Yamada

    发明人： Kaori Yoshida ,  Takeshi Ebisu ,  Eisaku Okubo ,  Katsuhiko Yamada

    IPC分类号： F28F308

    CPC分类号： F28F3/046 ,  F28D9/005 ,  F28F3/083 ,  F28F9/026 ,  Y10S165/368

    摘要： A plate-type heat exchanger is constructed by piling a plurality of heat transfer plates (P3) having an aspect ratio (=(longitudinal length (Y))/(lateral length (X))) of 1.5. The heat transfer plate (P3) is formed of a substantially planar plate in rectangular shape and has wave-shaped heat transfer enhancement surfaces (20a), (30a) formed on its surfaces. The four corners of the heat transfer plate, i.e., the lower left corner, the upper right corner, the upper left corner and the lower right corner, are formed with a first opening (21a) as an inlet of a first flow channel, a second opening (22a) as an outlet of the first flow channel, a third opening (23a) as an inlet of a second flow channel and a fourth opening (24a) as an outlet of the second flow channel, respectively. Around the openings (21a) through (24a), respective seals (12a) through (15a) are provided to rise toward the front side or the back side of the heat transfer plate. Each of the seals (12a) through (15a) is provided with a plurality of ribs (51) through (57) for suppressing a drift of refrigerant in the flow channel.

    摘要翻译： 板式热交换器通过将具有纵横比（=（纵向长度（Y））/（横向长度（X）））的多个传热板（P3）堆叠为1.5来构造。 传热板（P3）由大致平面的矩形形状的板形成，并且在其表面上形成有波浪状的传热增强面（20a），（30a）。 传热板的四角，即左下角，右上角，左上角和右下角形成有作为第一流动通道的入口的第一开口（21a）， 作为第一流动通道的出口的第二开口（22a），作为第二流动通道的入口的第三开口（23a）和作为第二流动通道的出口的第四开口（24a）。 在开口（21a）至（24a）的周围，各自的密封件（12a）至（15a）设置成朝向传热板的前侧或后侧上升。 每个密封件（12a）至（15a）设置有多个用于抑制流动通道中制冷剂漂移的肋（51）至（57）。