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    • 4. 发明专利
    • DE4201637A1
    • 1992-08-06
    • DE4201637
    • 1992-01-22
    • HITACHI LTD
    • TAKAHASHI FUMIOHARADA IWAOFUJITANI YASUOAIZAWA MICHIHIKO
    • F28B1/02F25B37/00F25B39/04F28B1/00F28B9/10F28D7/00F28F1/32G21D1/02
    • A heat exchanger for condensing into liquid phase a vapor containing non-condensable gas components through heat exchange with a heat exchanging medium has a vessel having a vapor inlet for receiving the vapor containing the non-condensable gas components and a discharge port for the non-condensable gas components. The heat exchanger further has a tube nest disposed in the vessel and having a plurality of tubes through which the heat exchanging medium flows. The vapor containing non-condensable gas components flows towards the discharge port across the tube nest so as to be condensed into liquid phase through heat exchange with the heat exchanging medium flowing through the tubes, so that the non-condensable gas components are separated from the liquid phase and flow towards the discharge port. The tube nest is constructed to create a change in the dynamic pressure of flow of the vapor towards the discharge port to cause such a static pressure distribution in the heat exchanger that a lower static pressure is established in a region where the discharge port is provided than in a region where the vapor inlet is provided.
    • 5. 发明专利
    • ABSORPTION TYPE COLD/HOT WATER GENERATOR
    • JPH11287527A
    • 1999-10-19
    • JP5661499
    • 1999-03-04
    • HITACHI LTD
    • URAKI YASUOKABETA AKIRANAKAO TAKESHIAIZAWA MICHIHIKOOUCHI TOMIHISA
    • F24F11/02F25B15/00
    • PROBLEM TO BE SOLVED: To provide an absorption type cold/hot water generator used in a multi type absorption air-conditioning system to perform comfortable air-conditioning and improve facility. SOLUTION: In an absorption cold/hot water generator, a weak solution dilluted by a refrigerant is heated by a high temperature regenerator 25 and a low temperature regenerator 24 to generate refrigerant steam and after, during cooling, refrigerant steam is cooled and condensed by a cooling means, the steam is evaporated by an evaporator 21. Further, during heating, cold/hot water is heated by using refrigerant steam by the evaporator 21 to produce hot water. A refrigerant to cool or heat cold/hot water by the evaporator 21 is absorbed or mixed in a strong solution generated during the generation of refrigerant steam by an absorber 22 to produce a weak solution, which is returned again to the high temperature regenerator 25 and the low temperature regenerator 24. The evaporator 21 and the absorber 22 are arranged in parallel, the condenser 23 and the low temperature regenerator 24 are arranged on the upper side of the evaporator 23 and the absorber 22. Further, the high temperature regenerator 25 is arranged in parallel to the evaporator 21 and the absorber 22. The evaporator apparatus 21 and the absorber 22, and the condenser 23 and the low temperature regenerator 24 are partitioned from each other by a partition plate 45. The partition plate 45 is bent and protruded between the condenser 23 and the low temperature regenerator 24 to form a heat insulation space.
    • 9. 发明专利
    • MIXED ABSORBING LIQUID AND ABSORPTION HEAT EXCHANGER USING THE SAME LIQUID
    • JPH04309756A
    • 1992-11-02
    • JP7540291
    • 1991-04-08
    • HITACHI LTD
    • KOSEKI YASUOKOIKE SEIJIAIZAWA MICHIHIKOYAMADA AKIRA
    • F25B15/00C09K5/04
    • PURPOSE:To embody the cooling operation by air cooling process or the heating operation by a heat pump using outside air as a heating source by a method wherein potassium salt such as potassium chloride is added in a specific proportion to the absorbing liquid consisting of lithium bromide as a main absorbing agent for use in an absorption heat exchange device. CONSTITUTION:In the cooling operation of an absorption heat exchange device, e.g. absorption air conditioning device, the water 26 being refrigerant is sprayed into a heat transfer pipe 100 of an evaporator 1 by a refrigerant pump 7 and, by the latent heat produced by the evaporation of the water 26, a cooling water 10 in the heat transfer pipe 100 is chilled and the cooling water 10 thus chilled is used for the cooling. The water vapor 25 also produced enters an absorber 2 and is absorbed by a mixed absorbing liquid 20 sprayed into a heat transfer pipe 101. The absorbing liquid 20 diluted by absorbing the water vapor 25 is sent into a heat exchanger 3 by an absorbing liquid pump 8 to be preheated, a part of the absorbing liquid is sent into a low temperature regenerator 5 and the remainder is sent into a high temperature regenerator 4. The absorbing liquid 20 consists of lithium bromide as a main absorbing agent with potassium salt added thereto.
    • 10. 发明专利
    • AIR BLEEDER
    • JPH0391665A
    • 1991-04-17
    • JP22438289
    • 1989-09-01
    • HITACHI LTD
    • AIZAWA MICHIHIKO
    • F25B43/04
    • PURPOSE:To make it possible to extract a noncondensible gas outside effectively and simplify the device and its components by installing a gas extraction tank whose surface is partially cooled with refrigerant a cold water, and a gas extraction pipeline which connects the gas extraction tank with a vapor phase section on the down stream side of a condenser. CONSTITUTION:A gas extraction tank 21 has its one side placed in contact with the surface of a refrigerant tank 4 or shares its side with the tank 4. The tank 21 is always cooled with a refrigerant solution which flows down along the wall of a vaporizer 1. Therefore, the internal pressure in the extraction tank 21 can be kept to a lower value substantially near to the internal pressure in the refrigerant tank 4. A gas extraction pipeline 22 is connected between a lower manifold 17 of an air-cooled condenser 15 and the gas extraction tank 21. Therefore, the noncondensible gas in the lower manifold 17 flows into the extraction gas tank 21 with vapor due to the difference between the pressures where only the vapor content is condensed and liquefied while the noncondensible gas is gradually built up inside the gas extraction tank 21. This construction makes it possible to extract the noncondensible gas in an absorption type refrigerator effectively outside and provide a gas extraction unit which is simple in structure and highly reliable in performance.