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    • 2. 发明专利
    • Absorption chiller
    • JP4903743B2
    • 2012-03-28
    • JP2008097135
    • 2008-04-03
    • 日立アプライアンス株式会社
    • 浩伸 川村伸之 武田達郎 藤居章 西口
    • F25B15/00F25B37/00F25B39/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To increase a piping-up temperature difference and to prevent leakage from a tube expanding section of a heat transfer tube in an absorption type refrigerating machine. SOLUTION: A low-temperature evaporator 17, a low-temperature absorber 11, a high-temperature evaporator 14 and a high-temperature absorber 6 are constituted of one can body 60. The low-temperature absorber 11 and the high-temperature evaporator 14 in which a plurality of the heat transfer tubes 16 are vertically disposed, disposed between the low-temperature evaporator 17 and the high-temperature absorber 6 in which the plurality of heat transfer tubes 19, 8 are horizontally disposed. A refrigerant liquid is supplied to each heat transfer tube from upper portions of the plurality of vertical heat transfer tubes 16. Can body both side faces over the low-temperature evaporator, the low-temperature absorber, the high-temperature evaporator and the high-temperature absorber are formed by using two sheets of first tube plates 50, 51. Both ends of the plurality of heat transfer tubes 19 of the low-temperature evaporator 17 and both ends of the plurality of heat transfer tubes 8 of the high-temperature absorber 6 are expanded and fixed to the two sheets of first tube plates 50, 51. COPYRIGHT: (C)2010,JPO&INPIT
    • 5. 发明专利
    • Absorption chiller
    • JP4249588B2
    • 2009-04-02
    • JP2003348988
    • 2003-10-08
    • 日立アプライアンス株式会社株式会社日立製作所
    • 正雄 今成浩伸 川村伸之 武田達郎 藤居章 西口
    • F25B15/00F25B33/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To smooth the dilution of a solution in the whole cycle in an absorption water cooler-heater by filling the solution in a heat transfer pipe group without making the solution quantity in an upper header excessive at the time of starting, and surely discharging the concentrated solution left in heat transfer pipes at the time of stopping. SOLUTION: This absorption water cooler-heater comprises a circulating type high-temperature regenerator 1, a gas-liquid separator 16, a high-temperature regenerator vapor pipe 15 and a solution bypass pipe 17. The circulating type high-temperature regenerator 1 comprises the upper header 14, a lower header 12, and the heat transfer pipe group 13 provided between the both, and is adapted so that a dilute solution is supplied to the lower header and guided into the heat transfer pipe group 13. The gas-liquid separator 16 is connected to the upper header 14 to separate a refrigerant vapor generated in the heat transfer pipe group 13 from the concentrated solution. The high-temperature regenerator vapor pipe 15 is adapted to guide the refrigerant vapor and the concentrated solution from the upper header 14 to the gas-liquid separator 16. The solution bypass pipe 17 is adapted to connect the upper header 14 to an outlet passage for the solution separated by the gas-liquid separator 16. COPYRIGHT: (C)2005,JPO&NCIPI
    • 8. 发明专利
    • Absorption heat pump equipment
    • JP5390426B2
    • 2014-01-15
    • JP2010024646
    • 2010-02-05
    • 日立アプライアンス株式会社東京瓦斯株式会社
    • 伸之 武田修一郎 内田章 西口武 横山清幸 森教之 西山
    • F25B15/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To obtain an absorption type heat pump device capable of simultaneously supplying cold water and hot water and having a high COP. SOLUTION: The absorption type heat pump device includes an evaporator 4, an absorber 5, a condenser 3, a low-temperature regenerator 2, a high-temperature regenerator 1, solution heat exchangers 61, 62, a solution pump 51 and a refrigerant pump 41. The absorption type heat pump device further includes: cold water piping 71 connecting the evaporator 4 with a cold water load 7 and supplying cold water cooled by the evaporator 4 to the cold water load 7; and hot water piping 81 connecting the absorber 5 and the condenser 3 with a hot water load 8 and supplying hot water of which temperature is raised by cooling the absorber 5 and the condenser 3 to the hot water load 8. Each of the evaporator 4 and the absorber 5 is formed to have multiple stages on a low stage side with low pressure and a high stage side with high pressure. Hot water from the hot water load 8 is made to flow from the high stage side absorber 5b to the low stage side absorber 5a with low pressure, sequentially. Concentrated solution from the high-temperature regenerator 1 and the low-temperature regenerator 2 is made to flow from the low stage side absorber 5a to the high stage side absorber 5b. COPYRIGHT: (C)2011,JPO&INPIT
    • 10. 发明专利
    • Absorption chiller
    • JP4281967B2
    • 2009-06-17
    • JP2005128863
    • 2005-04-27
    • 日立アプライアンス株式会社
    • 浩伸 川村伸之 武田達郎 藤居章 西口
    • F25B15/00F25B33/00
    • Y02A30/277Y02B30/62
    • PROBLEM TO BE SOLVED: To provide an absorption water cooler/heater capable of reducing solution quantity, shortening a starting time in starting an operation and a dilution time in stopping the operation, increasing a degree of freedom in installing an apparatus, surely supplying the solution even in starting and the like, and continuing the operation. SOLUTION: In this absorption water cooler/heater, an intermediate-temperature regenerator 11 is constituted by a falling liquid film-type regenerator to which the dilute solution of low concentration is sprayed from an upper portion of a pipe group 12 of the intermediate-temperature regenerator 11 through a spraying device 14. A liquid reservoir 15 is mounted at a solution outlet portion of the intermediate-temperature regenerator 11 to temporarily reserve the solution flowing out from the intermediate-temperature regenerator 11. Further a flow adjusting means is mounted for adjusting the flow of the solution sprayed to the pipe group 12 in the intermediate-temperature regenerator 11 in accordance with a height of a liquid level of the liquid reservoir 15. The flow adjusting means adjusts the solution to flow by the quantity more than that predetermined as an inflow quantity to the intermediate-temperature regenerator 11 when the height of liquid level of the liquid reservoir 15 reaches a height more than predetermined upper limit height. COPYRIGHT: (C)2007,JPO&INPIT