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    • 8. 发明授权
    • Absorption air-conditioning system
    • 吸收式空调系统
    • US5259202A
    • 1993-11-09
    • US827749
    • 1992-01-29
    • Akira NishiguchiTomihisa OhuchiDaisuke HisajimaMichihiko Aizawa
    • Akira NishiguchiTomihisa OhuchiDaisuke HisajimaMichihiko Aizawa
    • F25B15/00F25B15/06F25B49/04
    • F25B15/06F25B15/008F25B49/043F25B2315/001Y02B30/62
    • In an absorption air-conditioning system, in order to immediately stop indoor air-conditions by a stop signal of the indoor air-conditioners and improve characteristics for activating the system , such as, by effecting re-activation at a relatively short time interval after stopping the operation of the system, when the last one of the operating indoor air-conditioners is stopped, a stop signal is sent to a control device from a controller for the indoor air-conditioner, and in response to this signal, the control device effects the control of stopping a burner, a cooling medium circulating pump, a cooling water pump and a cold/hot water, pump. A solution circulating pump, however, continues operating and the solution, while kept at a high concentration, is circulated through an absorber, a high-temperature regenerator and a low-temperature regenerator. During this time, an indicated value of a temperature sensor gradually decreases, and when this value reaches a predetermined temperature, the control device switches a control valve from its open condition to its closed condition and another control valve from its closed condition to its open condition, and also activates the cooling medium circulating pump again to feed a cooling medium to a solution reservoir at a lower portion of the absorber, thereby diluting the solution.
    • 在吸收式空调系统中,为了通过室内空调的停止信号立即停止室内空调,提高启动系统的特性,例如通过在相对较短的时间间隔之后进行再激活,经过 停止系统的运转,当最后一个运行的室内空调机停止时,停止信号从室内空调器的控制器发送到控制装置,并且响应于该信号,控制装置 影响停止燃烧器,冷却介质循环泵,冷却水泵和冷/热水泵的控制。 然而,溶液循环泵继续运行,并且保持高浓度的溶液通过吸收器,高温再生器和低温再生器循环。 在此期间,温度传感器的指示值逐渐降低,当该值达到预定温度时,控制装置将控制阀从其打开状态切换到关闭状态,另一个控制阀从其关闭状态切换到打开状态 并且还再次激活冷却介质循环泵,以将冷却介质供给到吸收器下部的溶液储存器,从而稀释溶液。
    • 9. 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。
    • 10. 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。