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    • 2. 发明授权
    • Absorption refrigerating machine
    • 吸收式制冷机
    • US06122930A
    • 2000-09-26
    • US248129
    • 1999-02-10
    • Akira NishiguchiRyoko SakiyamaTomihisa OhuchiMichihiko Aizawa
    • Akira NishiguchiRyoko SakiyamaTomihisa OhuchiMichihiko Aizawa
    • F25B15/00F25B15/06
    • F25B15/008F25B15/06F25B2400/09Y02B30/62
    • There is disclosed an absorption refrigerating machine in which evaporators as well as absorbers are arranged in a two-stage manner. A refrigerant, heated by a regenerator, is condensed by a condenser, and then is fed to a first evaporator. The refrigerant, produced in the first evaporator, is absorbed by a first absorber, formed integrally with the first evaporator, and is formed into an intermediate solution, and then is fed to a second absorber. The second absorber comprises a spray absorber which obviates the need for providing a heat-transfer pipe therein. The condensed refrigerant is supplied to a second evaporator, formed integrally with the second absorber, from a refrigerant tank formed at a lower portion of the condenser or at a lower portion of the first evaporator. The refrigerant, fed to the second evaporator, is absorbed by the solution sprayed in a supercooled condition in the second absorber, thereby producing a dilute solution. Part of the dilute solution, raised in temperature by absorbing the refrigerant, is returned to the first evaporator, and exchanges heat with liquid refrigerant, condensed in the condenser, to be cooled. The cooled dilute solution is again sprayed in the second absorber. The dilute solution in the second absorber is kept in a supercooled condition, and therefore the chilled water or brine, flowing through a heat-transfer pipe, provided in the second evaporator, can be kept to a low temperature under 0.degree. C.
    • 公开了一种吸收式制冷机,其中蒸发器以及吸收器以两级方式排列。 由再生器加热的制冷剂通过冷凝器冷凝,然后被供给到第一蒸发器。 在第一蒸发器中产生的制冷剂由与第一蒸发器一体形成的第一吸收器吸收,并形成中间溶液,然后被供给到第二吸收器。 第二吸收器包括喷射吸收器,其不需要在其中提供传热管。 冷凝的制冷剂从形成在冷凝器的下部的制冷剂罐或第一蒸发器的下部供给到与第二吸收器一体形成的第二蒸发器。 供给到第二蒸发器的制冷剂被第二吸收器中以过冷却状态喷射的溶液吸收,从而产生稀溶液。 通过吸收制冷剂在温度升高的部分稀释溶液返回到第一蒸发器,与冷凝器中冷凝的液体制冷剂进行热交换以进行冷却。 冷却的稀释溶液再次喷洒在第二吸收器中。 将第二吸收器中的稀溶液保持在过冷状态,因此在第二蒸发器中流过传热管的冷冻水或盐水可以在0℃下保持在低温。
    • 3. 发明授权
    • High temperature regenerator of an absorption type hot and cold water
generator and absorption type hot and cold water generator
    • 吸收式冷热水发生器和吸收式冷热水发生器的高温再生器
    • US5435154A
    • 1995-07-25
    • US181022
    • 1994-01-14
    • Akira NishiguchiTomihisa OhuchiShigeo SugimotoMichihiko AizawaTakao NaruseYasuo Uraki
    • Akira NishiguchiTomihisa OhuchiShigeo SugimotoMichihiko AizawaTakao NaruseYasuo Uraki
    • F24H1/44F25B33/00F25B15/00
    • F24H1/40F24H1/26F24H1/44F25B33/00F25B2333/002F25B2333/003
    • A high temperature regenerator of an absorption type hot and cold water generator and an absorption type hot and cold water generator capable of preventing corrosion from occurring by preventing local overheating at the heat transfer surface of the high temperature regenerator and capable of being miniaturized. The high temperature regenerator includes an outer case, an inner case, a plurality of solution pipes, a burner, a solution flow-in pipe, and a gas/liquid separation plate. The inner case is inside the outer case, and a solution is kept between the cases, with the inner case being submerged within this solution. The burner is mounted on the side of the outer case in such a way that heat can be supplied through the inner case, with the inside of the inner case serving as a combustion chamber. A plurality of solution pipes, through which the upper and lower portions of the inner case are connected, are disposed downstream of the combustion chamber, and the inside of each of the solution pipes is filled with the solution. The horizontal cross section of each of the solution pipes is elliptical, and two or more of the solution pipes are disposed so that the straight line portions in the elliptical shape become parallel to each other. The sections between the solution pipes serve as a combustion gas passage.
    • 吸收式冷热水发生器的高温再生器和吸收型冷热水发生器,其能够通过防止高温再生器的传热面上的局部过热而防止腐蚀发生,并能够小型化。 高温再生器包括外壳,内壳,多个溶液管,燃烧器,溶液流入管和气/液分离板。 内壳在外壳的内部,溶液保持在壳体之间,内壳浸没在该溶液中。 燃烧器安装在外壳的侧面,使得可以通过内壳供应热量,内壳的内部用作燃烧室。 内壳体的上部和下部连接的多个溶液管设置在燃烧室的下游,并且每个溶液管的内部填充有溶液。 每个溶液管的水平截面是椭圆形的,并且两个或更多个溶液管被设置成使得椭圆形的直线部分彼此平行。 溶液管之间的部分用作燃烧气体通道。
    • 8. 发明授权
    • Absorption refrigerating machine
    • 吸收式制冷机
    • US06233968B1
    • 2001-05-22
    • US09618941
    • 2000-07-18
    • Akira NishiguchiRyoko SakiyamaTomihisa OhuchiMichihiko Aizawa
    • Akira NishiguchiRyoko SakiyamaTomihisa OhuchiMichihiko Aizawa
    • F25B1500
    • F25B15/008F25B15/06F25B2400/09Y02A30/277Y02B30/62
    • There is disclosed an absorption refrigerating machine in which evaporators as well as absorbers are arranged in a two-stage manner. A refrigerant, heated by a regenerator, is condensed by a condenser, and then is fed to a first evaporator. The refrigerant, produced in the first evaporator, is absorbed by a first absorber, formed integrally with the first evaporator, and is formed into an intermediate solution, and then is fed to a second absorber. The second absorber comprises a spray absorber which obviates the need for providing a heat-transfer pipe therein. The condensed refrigerant is supplied to a second evaporator, formed integrally with the second absorber, from a refrigerant tank formed at a lower portion of the condenser or at a lower portion of the first evaporator. The refrigerant, fed to the second evaporator, is absorbed by the solution sprayed in a supercooled condition in the second absorber, thereby producing a dilute solution. Part of the dilute solution, raised in temperature by absorbing the refrigerant, is returned to the first evaporator, and exchanges heat with liquid refrigerant, condensed in the condenser, to be cooled. The cooled dilute solution is again sprayed in the second absorber. The dilute solution in the second absorber is kept in a supercooled condition, and therefore the chilled water or brine, flowing through a heat-transfer pipe, provided in the second evaporator, can be kept to a low temperature under 0° C.
    • 公开了一种吸收式制冷机,其中蒸发器以及吸收器以两级方式排列。 由再生器加热的制冷剂通过冷凝器冷凝,然后被供给到第一蒸发器。 在第一蒸发器中产生的制冷剂由与第一蒸发器一体形成的第一吸收器吸收,并形成中间溶液,然后被供给到第二吸收器。 第二吸收器包括喷射吸收器,其不需要在其中提供传热管。 冷凝的制冷剂从形成在冷凝器的下部的制冷剂罐或第一蒸发器的下部供给到与第二吸收器一体形成的第二蒸发器。 供给到第二蒸发器的制冷剂被第二吸收器中以过冷却状态喷射的溶液吸收,从而产生稀溶液。 通过吸收制冷剂在温度升高的部分稀释溶液返回到第一蒸发器,与冷凝器中冷凝的液体制冷剂进行热交换以进行冷却。 冷却的稀释溶液再次喷洒在第二吸收器中。 将第二吸收器中的稀溶液保持在过冷状态,因此在第二蒸发器中流过传热管的冷冻水或盐水可以在0℃下保持在低温。