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    • 5. 发明专利
    • METHOD AND APPARATUS FOR COLD HEAT GENERATION
    • JPH02122170A
    • 1990-05-09
    • JP27195888
    • 1988-10-29
    • HITACHI LTD
    • YAMADA AKIRAOKOCHI ISAOKOSEKI YASUOKUROKAWA HIDEAKIEBARA KATSUYATAKAHASHI SANKICHIONODA TOSHISUKESUGIMOTO SHIGEO
    • F25B25/02F25B15/00
    • PURPOSE:To make an apparatus smaller in size by a method wherein heat storage medium is cooled by the ambient temperature and cold heat is generated by using the evaporation heat of refrigerant as a heat source after the refrigerant, circulating through a closed circuit of a compression type heat pump, is adiabatically expanded. CONSTITUTION:In case a concentration difference type heat storage apparatus 5 is brought in operation for cooling operation, concentrated lithium bromide solution from a heat storage medium storage 7 and from preceding stages is sprayed by spray pipes 561, 562 and 563, and an outdoor unit 9 and first heat exchangers 531, 532 and 533 are connected by pipes 312, 313, 314 and 315. When fleon is circulated by a pump 203 to cool the concentrated lithium bromide solution, the pressure in first compartments 511, 512 and 513 drops. On the other hand, the steam evaporated by third heat exchangers 551, 552 and 553 flows into second compartments 521, 522, and 523 through steam paths 591, 592 and 593, and absorbed by the concentrated lithium bromide solution with heat generation; however, the pressure in the first stage is lowest because the concentration of the lithium bromide solution sprayed by the distributor 561 of the first stage is highest. Therefore, as the concentration of the lithium bromide solution degrades in the order of the first stage, the second stage and third stage, the heat transfer area required can be reduced, resulting in a reduction in size of the apparatus.
    • 6. 发明专利
    • METHOD AND DEVICE FOR GENERATING COLD HEAT
    • JPH0252962A
    • 1990-02-22
    • JP19989288
    • 1988-08-12
    • HITACHI LTD
    • KOSEKI YASUOYAMADA AKIRAKUROKAWA HIDEAKIOKOCHI ISAOEBARA KATSUYATAKAHASHI SANKICHI
    • F25B15/00F25B15/06F25D16/00
    • PURPOSE:To improve cooling capacity by a method wherein, by using a suction cooling type freezer, a cold heat having temperature below a freezing point is generated, ice or ice slurry is generated for heat accumulation. CONSTITUTION:By heating a reproducer 12 by a heating source 20, e.g. combustion gas and steam, and cooling an absorber 11 and a condenser 13 by means of cooling water 21, brine (ethyleneglycol) 22 having temperature below a freezing point is produced from a vaporizer 10. An absorbent (LiBr) 15 is heated by the reproducer 12, a refrigerant (methanol) 14 is vaporized, and the absorbent 15 is concentrated to feed it to the absorber 11. The refrigerant steam 14 is cooled by the condenser 13 to produce liquid, which is fed to the vaporizer 10. As a result of the concentrated absorbent 15 in the absorber 11 being cooled, a pressure in a device is decreased. The reduction of a pressure causes vaporization of the refrigerant 14 in the vaporizer 10 under the same pressure, temperature is reduced to a value below a freezing point, and brine having temperature below a freezing point (approximately -6 deg.C) is produced from the vaporizer 10. Brine having temperature below a freezing point flows through a 3-way valve 33 and enters a heat accumulating tank 2, and water in the tank is indirectly cooled to produce ice.
    • 9. 发明专利
    • DOUBLE EFFECTIVE ABSORPTIVE TYPE REFRIGERATING CYCLE
    • JPH01208669A
    • 1989-08-22
    • JP2867788
    • 1988-02-12
    • HITACHI LTD
    • KOSEKI YASUOYAMADA AKIRAKUROKAWA HIDEAKIOKOCHI ISAOTAKAHASHI SANKICHIEBARA KATSUYA
    • F25B15/00
    • PURPOSE:To enable a direct air cooling to be performed and further enable a reutilization of cooling heat by a method wherein a low concentration absorbent is condensed by a hot regenerator and a high concentration absorbing agent is condensed by a low temperature regenerator, an absorption of refrigerant vapor from an evaporator is operated at a high pressure side of the hot temperature regenerator and at a low pressure side of a low temperature regenerator. CONSTITUTION:An absorbent 20a for lean and low concentration gas enters a high pressure part 1a of a hot regenerating unit, is heated and condensed and sent to a high pressure part 4a of an absorption unit as a high concentration and low concentration absorbent 22a. A coolant vapor 32a is absorbed to become a lean low concentration absorbent 20a and then sent to the high pressure part 1a again. The refrigerant vapors 30a and 30b generated at a high pressure part 1a and the low pressure part 1b are applied in heater sources of a high pressure part 2a and a low pressure part 2b and then sent to the evaporator as a refrigerant 30. The lean high concentration absorbent 20b enters the high pressure part 2a, heated and condensed, further condensed at the lower pressure part 2b and sent to the lower pressure part 4b of the absorber as the high concentration absorbent 22b. The absorbent absorbs the refrigerant vapor 32b to become the lean high concentration absorbent 20b and send to the higher pressure part 2a. The lower pressure part 5b of the evaporation unit provides a cold heat of 4 deg.C due to evaporation of refrigerant.