EP2930450A1 - Dispositif de conditionnement de l'air - Google Patents

Dispositif de conditionnement de l'air Download PDF

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Publication number
EP2930450A1
EP2930450A1 EP12889228.8A EP12889228A EP2930450A1 EP 2930450 A1 EP2930450 A1 EP 2930450A1 EP 12889228 A EP12889228 A EP 12889228A EP 2930450 A1 EP2930450 A1 EP 2930450A1
Authority
EP
European Patent Office
Prior art keywords
source side
heat source
side heat
refrigerant
heat exchanger
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP12889228.8A
Other languages
German (de)
English (en)
Other versions
EP2930450A4 (fr
EP2930450B1 (fr
Inventor
Takeshi Hatomura
Koji Yamashita
Shinichi Wakamoto
Naofumi Takenaka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
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Mitsubishi Electric Corp
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Filing date
Publication date
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Publication of EP2930450A1 publication Critical patent/EP2930450A1/fr
Publication of EP2930450A4 publication Critical patent/EP2930450A4/fr
Application granted granted Critical
Publication of EP2930450B1 publication Critical patent/EP2930450B1/fr
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B47/00Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
    • F25B47/02Defrosting cycles
    • F25B47/022Defrosting cycles hot gas defrosting
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/04Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
    • F28D1/0408Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
    • F28D1/0426Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
    • F28D1/0435Combination of units extending one behind the other
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/12Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element
    • F28F1/24Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely
    • F28F1/32Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only outside the tubular element and extending transversely the means having portions engaging further tubular elements
    • F28F1/325Fins with openings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/025Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units
    • F25B2313/0251Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units being defrosted alternately
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/025Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units
    • F25B2313/0253Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple outdoor units in parallel arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/031Sensor arrangements
    • F25B2313/0314Temperature sensors near the indoor heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/031Sensor arrangements
    • F25B2313/0315Temperature sensors near the outdoor heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/19Pressures
    • F25B2700/193Pressures of the compressor
    • F25B2700/1931Discharge pressures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/19Pressures
    • F25B2700/193Pressures of the compressor
    • F25B2700/1933Suction pressures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2104Temperatures of an indoor room or compartment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2106Temperatures of fresh outdoor air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2115Temperatures of a compressor or the drive means therefor
    • F25B2700/21152Temperatures of a compressor or the drive means therefor at the discharge side of the compressor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D2001/0253Particular components
    • F28D2001/026Cores
    • F28D2001/0273Cores having special shape, e.g. curved, annular
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0061Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0061Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • F28D2021/0063Condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0061Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for phase-change applications
    • F28D2021/0064Vaporizers, e.g. evaporators
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2215/00Fins
    • F28F2215/02Arrangements of fins common to different heat exchange sections, the fins being in contact with different heat exchange media
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2270/00Thermal insulation; Thermal decoupling

Definitions

  • the present invention relates to an air-conditioning apparatus.
  • a refrigerant circulates in a refrigerant circuit formed by connecting, by pipes, an outdoor unit as a heat source unit disposed outside a structure, for example, and an indoor unit disposed in the structure.
  • An air-conditioned space is heated or cooled by heating or cooling air by utilizing heat radiation or heat absorption of the refrigerant.
  • a heat exchanger of the outdoor unit serves as an evaporator and exchanges heat between a low-temperature refrigerant and air so that moisture in the air is condensed on fins and heat exchanger tubes of the heat exchanger, and frost is accumulated on the heat exchanger.
  • This frost accumulated on the heat exchanger blocks air passages of the heat exchanger and reduces the heat transfer area of the heat exchanger that performs heat exchange with air, resulting in a problem of a shortage of heating capacity.
  • a heating operation is stopped and a refrigerant flow switch valve is switched so that the heat exchanger of the outdoor unit serves as a condenser, and thereby, a defrosting operation is performed.
  • Such a defrosting operation can prevent a decrease in heating capacity.
  • a heating operation of the room is also stopped, and thus, the temperature in the room decreases and comfort in the indoor environments is impaired.
  • a typical technique performs a defrosting operation and a heating operation at the same time by using a plurality of outdoor heat exchangers and bypass pipes so as to allow a gas discharged from a compressor to be bypassed to the heat exchangers individually through shut-off valves and by operating some of the heat exchangers as evaporators and the other as condensers (see, for example, Patent Literature 1 and Patent Literature 2).
  • Patent Literature 1 and Patent Literature 2 uses outdoor heat exchangers, some of which performs a heating operation as evaporators and the other of which perform a defrosting operation as condensers, and the heating operation and the defrosting operation are performed at the same time.
  • outdoor heat exchangers some of which performs a heating operation as evaporators and the other of which perform a defrosting operation as condensers, and the heating operation and the defrosting operation are performed at the same time.
  • none of these literatures clearly describes the positional relationship among the heat exchangers.
  • Occurrence of the heat leakage reduces the defrosting capacity of the condenser near the interface between the evaporator and the condenser, resulting in insufficient defrosting near the interface.
  • the time necessary for the defrosting increases, the capacity of heating the room during a defrosting operation decreases, and comfort in the indoor environments is impaired.
  • water drops generated after the defrosting are frozen so that root ice is generated, the heat transfer area of the heat exchanger decreases, the heating capacity decreases, and the comfort in the indoor environments is impaired.
  • the present invention has been made in order to solve the above-described problems, and it is therefore an object of the invention to provide an air-conditioning apparatus that can reduce heat leakage through fins between adjacent heat exchangers.
  • An air-conditioning apparatus includes: a main circuit in which a compressor, a load side heat exchanger, a load side expansion device, and a plurality of heat source side heat exchangers connected in parallel are sequentially connected by pipes and in which a refrigerant circulates; a bypass pipe configured to cause part of a refrigerant discharged from the compressor to branch and flow into at least one of the plurality of heat source side heat exchangers to be defrosted; and a connection switching device configured to switch the one of the plurality of the heat source side heat exchangers to be defrosted by switching a channel of the bypass pipe between an open state and a closed state and switching a channel of the pipes of the main circuit connected to the plurality of heat source side heat exchangers between an open state and a closed state, wherein the heat source side heat exchanger includes a plurality of fins spaced apart from one another such that air passes between the plurality of fins, and a plurality of heat exchanger tubes disposed in the plurality of fins and
  • heat leakage through fins can be reduced between adjacent heat source side heat exchangers.
  • generation of remaining frost and root ice can be reduced in the interface between adjacent ones of the heat source side heat exchangers.
  • an air-conditioning apparatus that can achieve comfort in the indoor environments by reducing a defrosting time and a decrease in heating capacity can be obtained.
  • Fig. 1 is a circuit diagram schematically illustrating an example circuit configuration of an air-conditioning apparatus 100 according to Embodiment 1 of the present invention.
  • FIG. 1 the configuration of the air-conditioning apparatus 100 will be specifically described.
  • the air-conditioning apparatus 100 includes an outdoor unit 1 and an indoor unit 2, and the outdoor unit 1 and the indoor unit 2 are connected to each other by refrigerant main pipe 4.
  • the air-conditioning apparatus 100 circulates a refrigerant therein so that air-conditioning is performed by using a refrigeration cycle.
  • the air-conditioning apparatus 100 is configured to select a mode from a cooling-only operation mode in which all the operating indoor units 2 perform cooling, a heating-only operation mode in which all the operating indoor units 2 perform heating, and a defrosting operation mode in which the indoor units 2 defrost heat exchange units in the outdoor unit 1 while continuing a heating operation.
  • the outdoor unit 1 includes a compressor 10, a refrigerant channel switching device 11 such as a four-way valve, a heat source side heat exchanger 12a, a heat source side heat exchanger 12b, an accumulator 13, refrigerant pipes 3, and a hot gas bypass pipe 5.
  • the compressor 10, the refrigerant channel switching device 11 such as a four-way valve, the heat source side heat exchanger 12a, the heat source side heat exchanger 12b, and the accumulator 13 are connected together by the refrigerant pipes 3.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are connected in parallel to each other by the refrigerant pipes 3.
  • Second opening/closing devices 31 a and 31 b are provided to portions of the refrigerant pipes 3 connected to the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, the portions of the refrigerant pipes 3 connecting to a load side expansion device 22.
  • the hot gas bypass pipe 5 branches part of a high-temperature refrigerant discharged from the compressor 10, and allows the refrigerant to flow into a defrosting-target heat source side heat exchanger 12 of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b.
  • an end of the hot gas bypass pipe 5 is connected to the refrigerant pipe 3 between a discharge part of the compressor 10 and the refrigerant channel switching device 11.
  • the other end of the hot gas bypass pipe 5 is divided into two parts, one of which is connected to the refrigerant pipe 3 between the heat source side heat exchanger 12a and the second opening/closing device 31 a and the other is connected to the refrigerant pipe 3 between the heat source side heat exchanger 12b and the second opening/closing device 31 b.
  • the hot gas bypass pipe 5 connected to the heat source side heat exchanger 12a is provided with a first opening/closing device 30a.
  • the hot gas bypass pipe 5 connected to the heat source side heat exchanger 12b is provided with a first opening/closing device 30b.
  • the first opening/closing device 30a, the first opening/closing device 30b, the second opening/closing device 31 a, and the second opening/closing device 31 b of Embodiment 1 constitute "connection switching devices" of the invention.
  • the compressor 10 sucks a refrigerant therein, and compresses the refrigerant into a high-temperature high-pressure state.
  • the compressor 10 is, for example, an inverter compressor whose capacity can be controlled.
  • the refrigerant channel switching device 11 switches a refrigerant flow between a flow in the heating-only operation mode and a flow in the cooling-only operation mode.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b serve as evaporators in the heating-only operation mode, and serve as condensers in the cooling-only operation mode.
  • one of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b serves as an evaporator, and the other serves as a condenser.
  • Fig. 2 schematically illustrates an example configuration of heat source side heat exchangers placed in an outdoor unit in the air-conditioning apparatus 100 of Embodiment 1.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed in a casing 51 of the outdoor unit 1.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b include a plurality of fins spaced from each other to allow air to pass threrethrough and a plurality of heat exchanger tubes disposed among the fins and allowing a refrigerant to flow therethrough.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b exchange heat between air from air-sending devices such as the a fan 52 and a refrigerant.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed adjacent to each other such that the fins are oriented in the same direction.
  • the heat source side heat exchanger 12a is located above the heat source side heat exchanger 12b.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed side by side along the direction of stages, that is, the stage direction, of the heat exchanger tubes.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed one above the other such that the fins of the exchangers 12a and 12b are oriented in an identical direction.
  • a heat leakage reducing mechanism for reducing the amount of heat leakage between the adjacent heat source side heat exchangers 12a and 12b is provided between adjacent fins. Detailed description will be given later.
  • the accumulator 13 is provided at a suction side of the compressor 10, and stores a surplus refrigerant generated by the difference in operating state between the heating-only operation mode and the cooling-only operation mode and a surplus refrigerant generated by a transient change in operation.
  • the first opening/closing device 30a is a shut-off valve for causing a high-temperature refrigerant from the hot gas bypass pipe 5 to flow into the heat source side heat exchanger 12a when the heat source side heat exchanger 12a operates as a condenser in the defrosting operation mode.
  • the first opening/closing device 30b is a shut-off valve for causing a high-temperature refrigerant from the hot gas bypass pipe 5 to flow into the heat source side heat exchanger 12b when the heat source side heat exchanger 12b operates as a condenser in the defrosting operation mode.
  • the first opening/closing devices 30a and 30b are, for example, two way valves, solenoid valves, and electronic expansion valves, which can open and close refrigerant channels.
  • the second opening/closing device 31 a is a shut-off valve for shutting off a refrigerant channel in order to prevent a low-temperature two-phase refrigerant flowing out of the indoor unit 2 into the outdoor unit 1 through a refrigerant main pipe 4 from flowing into the heat source side heat exchanger 12a when the heat source side heat exchanger 12a operates as a condenser in the defrosting operation mode.
  • the second opening/closing device 31 b is a shut-off valve for shutting off a refrigerant channel in order to prevent a low-temperature two-phase refrigerant flowing out of the indoor unit 2 into the outdoor unit 1 through the refrigerant main pipe 4 from flowing into the heat source side heat exchanger 12b when the heat source side heat exchanger 12b operates as a condenser in the defrosting operation mode.
  • the second opening/closing devices 31 a and 31 b are, for example, two way valves, solenoid valves, and electronic expansion valves, which can open and close refrigerant channels.
  • the outdoor unit 1 includes a first pressure sensor 41 and a second pressure sensor 42, as pressure detection means.
  • the first pressure sensor 41 is provided to the pipe between the compressor 10 and the refrigerant channel switching device 11.
  • the first pressure sensor 41 detects the pressure of a high-temperature high-pressure refrigerant discharged from the compressor 10.
  • the second pressure sensor 42 is provided to the pipe between the refrigerant channel switching device 11 and the accumulator 13.
  • the second pressure sensor 42 detects the pressure of a low-pressure refrigerant to be sucked into the compressor 10.
  • the outdoor unit 1 includes, as temperature detection means, a first temperature sensor 43, a second temperature sensor 45, a third temperature sensor 48a, and a third temperature sensor 48b.
  • the first temperature sensor 43, the second temperature sensor 45, the third temperature sensor 48a, and the third temperature sensor 48b are, for example, thermistors.
  • the first temperature sensor 43 is provided to the pipe between the compressor 10 and the refrigerant channel switching device 11.
  • the first temperature sensor 43 measures the temperature of a refrigerant discharged from the compressor 10.
  • the second temperature sensor 45 is provided to an air inlet of one of the heat source side heat exchanger 12a or the heat source side heat exchanger 12b.
  • the second temperature sensor 45 measures the temperature of the air around the outdoor unit 1.
  • the third temperature sensor 48a is provided to the pipe between the heat source side heat exchanger 12a and the refrigerant channel switching device 11.
  • the third temperature sensor 48a measures the temperature of a refrigerant that has flowed from the heat source side heat exchanger 12a operating as an evaporator.
  • the third temperature sensor 48b is provided to the pipe between the heat source side heat exchanger 12b and the refrigerant channel switching device 11.
  • the third temperature sensor 48b measures the temperature of a refrigerant that has flowed from the heat source side heat exchanger 12b operating as an evaporator.
  • the indoor unit 2 includes a load side heat exchanger 21 and a load side expansion device 22.
  • the load side heat exchanger 21 is connected to the outdoor unit 1 through the refrigerant main pipe 4 so that a refrigerant flows in or out of the load side heat exchanger 21.
  • the load side heat exchanger 21 exchanges heat between air from an air-sending device such as a fan and a refrigerant.
  • the load side heat exchanger 21 generates air for heating or air for cooling to be supplied to an interior space.
  • the load side expansion device 22 has functions of a pressure reducing valve and an expansion valve, and reduces the pressure of a refrigerant and expands the refrigerant.
  • the load side expansion device 22 is located upstream of the load side heat exchanger 21 in a refrigerant flow in the cooling-only operation mode.
  • the load side expansion device 22 is a valve whose opening degree is variable by control.
  • the load side expansion device 22 is, for example, an electronic expansion valve.
  • the indoor unit 2 includes, as temperature detection means, a fourth temperature sensor 46, a fifth temperature sensor 47, and a sixth temperature sensor 44.
  • the fourth temperature sensor 46, the fifth temperature sensor 47, and the sixth temperature sensor 44 are, for example, thermistors.
  • the fourth temperature sensor 46 is provided to the pipe between the load side expansion device 22 and the load side heat exchanger 21.
  • the fourth temperature sensor 46 detects the temperature of a refrigerant flowing in the load side heat exchanger 21 or a refrigerant that has flowed from the load side heat exchanger.
  • the fifth temperature sensor 47 is provided to the pipe between the load side heat exchanger 21 and the refrigerant channel switching device 11 of the outdoor unit 1.
  • the fifth temperature sensor 47 detects the temperature of a refrigerant flowing in the load side heat exchanger 21 or a refrigerant that has flowed from the load side heat exchanger 21.
  • the sixth temperature sensor 44 is provided at the air inlet of the load side heat exchanger 21.
  • the sixth temperature sensor 44 detects an ambient air temperature in the room.
  • the compressor 10 the refrigerant channel switching device 11, the load side heat exchanger 21, the load side expansion device 22, and the heat source side heat exchangers 12a and 12b connected in parallel are sequentially connected to one another by pipes, and constitute a main circuit in which a refrigerant circulates.
  • one indoor unit 2 is connected to the outdoor unit 1 through the refrigerant main pipe 4, but the invention is not limited to this configuration.
  • a plurality of indoor units 2 may be connected in parallel to the outdoor unit 1.
  • the control device 50 is a microcomputer, and the air-conditioning apparatus 100 includes the control device 50 that is the microcomputer. Based on detection information obtained by the detection means and an instruction from a remote controller, the control device 50 controls the driving frequency of the compressor 10, the rotation speed (including ON/OFF) of the air-sending device, switching of the refrigerant channel switching device 11, opening/closing of the first opening/closing devices 30a and 30b, opening/closing of the second opening/closing device 31, and the opening degree of the load side expansion device 22, for example, and performs operation modes described later.
  • the control device 50 may be provided to each unit, or may be provided to the outdoor unit 1 or the indoor unit 2.
  • Fig. 3 is a refrigerant circuit diagram showing a refrigerant flow in a cooling-only operation mode of the air-conditioning apparatus 100 of Embodiment 1.
  • Fig. 3 shows a cooling-only operation mode using a case where a cooling energy load is generated in the load side heat exchanger 21 as an example.
  • the flow direction of a refrigerant is indicated by solid arrow lines.
  • the refrigerant channel switching device 11 is switched to a state indicated by the solid lines in Fig. 3 .
  • the first opening/closing device 30a and the first opening/closing device 30b are switched to closed states, and shut off the refrigerant.
  • the second opening/closing device 31 a and the second opening/closing device 31 b are switched to open states, and allow the refrigerant to pass therethrough.
  • a low-temperature low-pressure refrigerant is compressed and becomes a high-temperature high-pressure gas refrigerant, and the resulting refrigerant is discharged.
  • the high-temperature high-pressure gas refrigerant discharged from the compressor 10 flows into the heat source side heat exchanger 12a and the heat source side heat exchanger 12b through the refrigerant channel switching device 11.
  • the high-temperature high-pressure gas refrigerant that has flowed into the heat source side heat exchanger 12a and the heat source side heat exchanger 12b dissipates heat to the outdoor air in the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, and becomes a high-pressure liquid refrigerant.
  • the high-pressure liquid refrigerant that has flowed from the heat source side heat exchanger 12a and the heat source side heat exchanger 12b merge through the second opening/closing device 31 a and the second opening/closing device 31 b, and the resulting refrigerant flows out of the outdoor unit 1.
  • the high-pressure liquid refrigerant from the outdoor unit 1 flows into the indoor unit 2 through the refrigerant main pipe 4, expands in the load side expansion device 22, and becomes a low-temperature low-pressure two-phase refrigerant.
  • This two-phase refrigerant flows into the load side heat exchanger 21 operating as an evaporator, receives heat from the indoor air so as to cool the indoor air, and becomes a low-temperature low-pressure gas refrigerant.
  • the gas refrigerant that has flowed from the load side heat exchanger 21 flows into the outdoor unit 1 again through the refrigerant main pipe 4.
  • the refrigerant that has flowed into the outdoor unit 1 is sucked into the compressor 10 again through the refrigerant channel switching device 11 and the accumulator 13.
  • the control device 50 controls the opening degree of the load side expansion device 22 such that the degree of superheat obtained as the difference between the temperature detected by the fourth temperature sensor 46 and the temperature detected by the fifth temperature sensor 47 is constant.
  • Fig. 4 is a refrigerant circuit diagram showing a refrigerant flow in a heating-only operation mode of the air-conditioning apparatus 100 of Embodiment 1.
  • Fig. 4 shows a heating-only operation mode using a case where a heating energy load is generated in the load side heat exchanger 21 as an example.
  • the flow direction of a refrigerant is indicated by solid arrow lines.
  • the refrigerant channel switching device 11 is switched to a state indicated by the solid lines in Fig. 4 .
  • the first opening/closing device 30a and the first opening/closing device 30b are switched to closed states, and shut off the refrigerant.
  • the second opening/closing device 31 a and the second opening/closing device 31 b are switched to an open state, and allow the refrigerant to pass therethrough.
  • the compressor 10 When the compressor 10 is driven, the low-temperature low-pressure refrigerant is compressed and becomes a high-temperature high-pressure gas refrigerant, and the resulting refrigerant is discharged.
  • the high-temperature high-pressure gas refrigerant discharged from the compressor 10 flows out of the outdoor unit 1 through the refrigerant channel switching device 11.
  • the high-temperature high-pressure gas refrigerant that has flowed from the outdoor unit 1 flows into the indoor unit 2 through the refrigerant main pipe 4, transfers heat to the indoor air in the load side heat exchanger 21, and thereby, becomes a liquid refrigerant while heating the indoor air.
  • the low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant that has flowed into the outdoor unit 1 flows into the heat source side heat exchanger 12a and the heat source side heat exchanger 12b through the second opening/closing device 31 a and the second opening/closing device 31 b, respectively.
  • the refrigerant that has flowed into each of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b absorbs heat from the outdoor air and becomes a low-temperature low-pressure gas refrigerant, and the resulting refrigerant is sucked into the compressor 10 again through the refrigerant channel switching device 11 and the accumulator 13.
  • the control device 50 controls the opening degree of the load side expansion device 22 such that the degree of subcooling obtained as the difference between a value of a saturation temperature converted from the pressure detected by the first pressure sensor 41 and the temperature detected by the fourth temperature sensor 46.
  • a defrosting operation mode is performed when detection results of the third temperature sensors 48a and 48b at the outlets of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are less than or equal to a predetermined value. Specifically, when the heating-only operation is performed so that the detection results of the third temperature sensors 48a and 48b decrease to a predetermined value or less (e.g., about -10 degrees C or less), the control device 50 determines that a predetermined amount of frost is accumulated on the fins of the heat source side heat exchangers 12a and 12b, and the defrosting operation is performed.
  • a predetermined value or less e.g., about -10 degrees C or less
  • the heat source side heat exchanger 12b located in a lower space of the casing 51 is defrosted, and then the heat source side heat exchanger 12a located in an upper space of the casing 51 is defrosted.
  • One of the heat source side heat exchanger 12a or the heat source side heat exchanger 12b that is not a defrosting target operates as an evaporator, and the load side heat exchanger 21 of the indoor unit 2 operates as a condenser. In this manner, the heating operation continues.
  • Fig. 5 is a refrigerant circuit diagram showing a refrigerant flow in a case where the heat source side heat exchanger 12b is defrosted in the defrosting operation mode of the air-conditioning apparatus 100 of Embodiment 1.
  • the flow direction of a refrigerant is indicated by solid arrow lines.
  • the refrigerant channel switching device 11 In the defrosting operation mode, the refrigerant channel switching device 11 is maintained in a state indicated by solid lines in Fig. 5 .
  • the first opening/closing device 30b is switched to an open state and allows a refrigerant to pass therethrough.
  • the second opening/closing device 31 b is switched to a closed state and shuts off the refrigerant.
  • the first opening/closing device 30a is maintained in a closed state and shuts off the refrigerant.
  • the second opening/closing device 31 a is maintained in an open state and allows the refrigerant to pass therethrough.
  • the low-temperature low-pressure refrigerant is compressed and becomes a high-temperature high-pressure gas refrigerant, and the resulting refrigerant is discharged.
  • Part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 passes through the hot gas bypass pipe 5, and flows into the heat source side heat exchanger 12b through the first opening/closing device 30b.
  • the high-temperature high-pressure gas refrigerant that has flowed into the heat source side heat exchanger 12b becomes a low-temperature gas refrigerant while melting frost on the heat source side heat exchanger 12b, and merges with a refrigerant that has flowed from the heat source side heat exchanger 12a.
  • the other part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 flows out of the outdoor unit 1 through the refrigerant channel switching device 11.
  • the high-temperature high-pressure gas refrigerant that has flowed from the outdoor unit 1 flows into the indoor unit 2 through the refrigerant main pipe 4, transfers heat to the indoor air in the load side heat exchanger 21, and becomes a liquid refrigerant while heating the indoor air.
  • the low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant that has flowed into the outdoor unit 1 flows into the heat source side heat exchanger 12a through the second opening/closing device 31 a.
  • the refrigerant that has flowed into the heat source side heat exchanger 12a absorbs heat from the outdoor air, and becomes a low-temperature low-pressure gas refrigerant.
  • the gas refrigerant that has flowed from the heat source side heat exchanger 12a merges with the gas refrigerant that has flowed from the heat source side heat exchanger 12b, and is sucked into the compressor 10 again through the refrigerant channel switching device 11 and the accumulator 13.
  • the control device 50 finishes defrosting of the heat source side heat exchanger 12b.
  • the predetermined time can be a time until all the frost melts in a case where frost is accumulated over the entire heat source side heat exchanger 12b without a clearance and part of the high-temperature high-pressure refrigerant flows into the heat source side heat exchanger 12b.
  • Fig. 6 is a refrigerant circuit diagram showing a refrigerant flow in a case where the heat source side heat exchanger 12a is defrosted in the defrosting operation mode of the air-conditioning apparatus 100 of Embodiment 1.
  • the flow direction of a refrigerant is indicated by solid arrow lines.
  • the refrigerant channel switching device 11 In the defrosting operation mode, the refrigerant channel switching device 11 is maintained in a state indicated by the solid lines in Fig. 6 .
  • the first opening/closing device 30a is switched to an open state and allows a refrigerant to pass therethrough.
  • the second opening/closing device 31 a is switched to a closed state and shuts off the refrigerant.
  • the first opening/closing device 30b is switched to a closed state and shuts off the refrigerant.
  • the second opening/closing device 31 b is switched to an open state and allows the refrigerant to pass therethrough.
  • the low-temperature low-pressure refrigerant is compressed and becomes a high-temperature high-pressure gas refrigerant, and the resulting refrigerant is discharged.
  • Part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 passes through the hot gas bypass pipe 5, and flows into the heat source side heat exchanger 12a through the first opening/closing device 30a.
  • the high-temperature high-pressure gas refrigerant that has flowed into the heat source side heat exchanger 12a becomes a low-temperature gas refrigerant while melting frost attached to the heat source side heat exchanger 12a, and merges with a refrigerant that has flowed from the heat source side heat exchanger 12b.
  • the other part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 flows out of the outdoor unit 1 through the refrigerant channel switching device 11.
  • the high-temperature high-pressure gas refrigerant that has flowed out of the outdoor unit 1 flows into the indoor unit 2 through the refrigerant main pipe 4, transfers heat to the indoor air in the load side heat exchanger 21, and becomes a liquid refrigerant while heating indoor air.
  • the liquid refrigerant that has flowed out of the load side heat exchanger 21 expands in the load side expansion device 22 and becomes a low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant, and the resulting refrigerant flows into the outdoor unit 1 again through the refrigerant main pipe 4.
  • the low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant that has flowed into the outdoor unit 1 flows into the heat source side heat exchanger 12b through the second opening/closing device 31 b.
  • the refrigerant that has flowed into the heat source side heat exchanger 12b absorbs heat from the outdoor air and becomes a low-temperature low-pressure gas refrigerant.
  • the gas refrigerant that has flowed out of the heat source side heat exchanger 12b merges with a gas refrigerant that has flowed from the heat source side heat exchanger 12a, and is sucked into the compressor 10 again through the refrigerant channel switching device 11 and the accumulator 13.
  • the control device 50 finishes defrosting of the heat source side heat exchanger 12a.
  • the predetermined time can be a time until all the frost melts in a case where frost is accumulated over the entire heat source side heat exchanger 12a without a clearance and part of the high-temperature high-pressure refrigerant flows into the heat source side heat exchanger 12a.
  • Performing the defrosting operation mode in this manner can defrost the heat source side heat exchangers 12a and 12b while continuing the heating operation.
  • the heat source side heat exchanger 12b located in the lower space of the casing 51 is defrosted, and then the heat source side heat exchanger 12a located in the lower space of the casing 51 is defrosted.
  • the heat source side heat exchanger 12b is defrosted, and then the heat source side heat exchanger 12a is defrosted.
  • the invention is not limited to this example.
  • the heat source side heat exchanger 12a may be first defrosted.
  • Fig. 7 schematically illustrates an example configuration in which the fins of the heat source side heat exchangers are not shared but are separated in the air-conditioning apparatus 100 of Embodiment 1.
  • reference numeral 61 denotes a fin of the heat source side heat exchanger 12a.
  • Reference numeral 64 denotes a heat transmission pipe of the heat source side heat exchanger 12a.
  • Reference numeral 62 denotes a fin of the heat source side heat exchanger 12b.
  • Reference numeral 65 denotes a heat transmission pipe of the heat source side heat exchanger 12b.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed one above the other (in the stage direction).
  • the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a is separated from the uppermost end face of the fin 62 of the lower heat source side heat exchanger 12b.
  • the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a is in contact with the lowermost end face of the fin 62 of the lower heat source side heat exchanger 12b at an interface 63.
  • the end face of each of the fin 61 and the fin 62 is subjected to a roughening process and forms a heat leakage reducing mechanism.
  • the roughening process only needs to be performed on the end face of at least one of the fin 61 or the fin 62 in the interface 63.
  • the heat leakage reducing mechanism causes the fin 61 and the fin 62 to be partially in contact with each other in the interface 63.
  • the amount of heat leakage from the condenser to the evaporator by thermal conduction between the fin 61 and the fin 62 can be reduced as compared to a case where the fin 61 and the fin 62 are integrated (shared).
  • the heat leakage amount Q1 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is expressed as Equation (1) of the amount of heat exchange due to typical thermal conduction.
  • T1 [degrees C] is a refrigerant gas temperature of the heat source side heat exchanger 12 serving as a condenser in the heat source side heat exchangers 12a and 12b;
  • T2 [degrees C] is a two-phase refrigerant temperature at the inlet of the heat source side heat exchanger 12 serving as an evaporator of the heat source side heat exchangers 12a and 12b;
  • ⁇ [W/mK] a thermal conductivity of a fin;
  • ⁇ [m] is an inter-fin distance indicating the distance between an end of a heat transmission pipe of the heat source side heat exchanger 12a near the interface 63 and an end of a heat transmission pipe of the heat source side heat exchanger 12b near the interface 63;
  • a [m 2 ] is an area calculated by multiplying the fin width [m], a fin thickness [m], and the number of fins.
  • the heat leakage amount Q1 in a case where the fin 61 and the fin 62 are integrated (shared) will be discussed.
  • the mean temperature T1 of a gas refrigerant flowing in the condenser performing defrosting is 20 degrees C and the temperature T2 of a refrigerant flowing in the evaporator used in heating operation is -15 degrees C.
  • the inter-fin distance ⁇ between the heat transmission pipe end of the evaporator and the heat transmission pipe end of the condenser in the interface 63 is 12.5 mm, and in a state where the heat exchangers are not separated, the fin width is 17 mm, the fin thickness is 0.1 mm, and the number of fins is 3700.
  • the heat leakage amount Q1 from the condenser to the evaporator in a case where the fins are not separated and are shared is about 3.60 kW from Equation (1).
  • the overall heat transfer coefficient is a half of the product of a heat transfer area (a contact area) and the overall heat transfer coefficient in a case where the fins are shared.
  • the heat leakage amount Q1 from the condenser to the evaporator due to thermal conduction of the fins is reduced, as compared to the case where all the fins are shared, by about 25% or more, and the heat leakage amount Q1 is about 2.7 kW.
  • the reason why the heat leakage amount Q1 is not reduced to a half of that of a case where all the fins are shared is the influence of temperature distribution in the fins.
  • the quantity of heat Q2 (calculated by multiplying latent heat of melting frost and the weight of frost) necessary for melting frost accumulated on the evaporator is about 1.5 MJ
  • the heat exchange amount Q3 between frost and a refrigerant used in defrosting in a case where no heat leakage amount is present from the condenser to the evaporator by thermal conduction of the fins is about 5.5 kW.
  • the time required for completion of defrosting is obtained by subtracting the difference between the heat exchange amount Q3 and the heat leakage amount Q1 from the solution heat amount Q2 of frost.
  • the heat leakage amount Q1 is reduced by about 25% to be about 2.7 kW, and suppose the heat exchange amounts Q2 and Q3 are under the above conditions, the time required for completion of defrosting is about 9 minutes.
  • the time required for completion of defrosting can be reduced by about 4 minutes.
  • the reduction of the time required for completion of defrosting enables part of a refrigerant discharged from the compressor 10 for defrosting to be quickly used for heating, as compared to a case where heat leakage occurs from the condenser to the evaporator by thermal conduction of the fins.
  • a decrease in heating capacity can be reduced.
  • a temperature decrease in the room can be reduced, thereby comfort of the indoor environments can be obtained.
  • a temperature decrease is reduced in the fin at the condenser side of the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, and thus, adfreezing of water drops generated by defrosting of the upper heat exchanger serving as the condenser can be reduced, thereby reducing generation of root ice.
  • Fig. 8 schematically illustrates an example configuration in which the fins of the heat source side heat exchangers are not shared but are separated and a notch is provided in the air-conditioning apparatus 100 of Embodiment 1.
  • a notch 66 is formed in part of the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a or part of the uppermost end face of the fin 62 of the lower heat source side heat exchanger 12b.
  • the notch 66 constitutes a heat leakage reducing mechanism.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed one above the other (in the stage direction).
  • the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a is separated from the uppermost end face of the fin 62 of the lower heat source side heat exchanger 12b.
  • the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a is in contact with the uppermost end face of the fin 62 of the lower heat source side heat exchanger 12b in the interface 63.
  • the notch 66 formed in part of the fins in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b can reduce the contact area of the fins in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, as compared to the case illustrated in Fig. 7 .
  • the heat leakage amount from the condenser to the evaporator by thermal conduction of the fins can be further reduced.
  • the thermal conductivity of the air is much lower than that of a material (e.g., aluminum) for the fins.
  • the thermal conductivity of the air is about 0.026 [W/(m ⁇ K)], whereas the thermal conductivity of aluminum is about 200 [W/(m ⁇ K)].
  • the amount of heat leakage caused by thermal conduction of the air is less than 1 % of the amount of heat leakage caused by thermal conduction of aluminum as a material for the fin, and the advantage of heat leakage reduction can be sufficiently obtained.
  • the height of the notch 66 of the fin is greater than or equal to about 0.1 mm, for example.
  • the width i.e., the horizontal direction
  • the heat leakage amount decreases.
  • the width may be determined such that the notch 66 is not crushed by the weight of the upper heat source side heat exchanger 12a of the heat source side heat exchangers 12 in the stage direction.
  • the width of the notch 66 can be a half or more of the width of the fin. In this case, defrosting can be performed without remaining frost.
  • FIG. 9 schematically illustrates an example configuration in which part of the fins of the heat source side heat exchangers is shared and a notch is provided in the air-conditioning apparatus 100 of Embodiment 1.
  • the fin 61 of the upper heat source side heat exchanger 12a and the fin 62 of the lower heat source side heat exchanger 12b are integrated (shared). That is, the fin 61 and the fin 62 are not separated but are shared.
  • a notch 66 is formed in part of the interface 63 between the fins at the lowermost heat transmission pipe 64 of the upper heat source side heat exchanger 12a and the uppermost heat transmission pipe 65 of the lower heat source side heat exchanger 12b.
  • the notch 66 constitutes a heat leakage reducing mechanism.
  • the configuration in which part of the fins is shared and the notch 66 is provided in the interface 63 between the fins enables the heat source side heat exchanger 12a and the heat source side heat exchanger 12b to be fabricated at the same time.
  • the number of fabrication processes can be reduced, and the cost for fabricating the heat source side heat exchangers 12 can be reduced.
  • Fig. 10 schematically illustrates an example configuration in which part of the fins of the heat source side heat exchangers is shared and a slit is provided in the air-conditioning apparatus 100 of Embodiment 1.
  • the fin 61 of the heat source side heat exchanger 12a and the fin 62 of the heat source side heat exchanger 12b are integrated (shared), and the fins are subjected to a process (a lancing process) such that parts of the fins at the ends of the notch are not cut off and remain in the interface 63 between the fins, thereby forming a slit 67.
  • the slit 67 constitutes a heat leakage reducing mechanism.
  • Such a configuration as described above allows a space to be formed in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, and thus, can obtain advantages similar to those of the configurations illustrated in Figs. 7 , 8, and 9 .
  • Fig. 11 schematically illustrates an example configuration in which the fins of the heat source side heat exchangers are not shared but are separated and an ellipsoidal notch is provided in the air-conditioning apparatus 100 of Embodiment 1.
  • the shape of the notch 66 or the slit 67 of the fins in the interface between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is not limited the rectangles illustrated in Figs. 7 , 8 , and 10 as long as a space is present in a portion of the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b where the fins are in contact with each other.
  • the shape may be various shapes such as a semi-ellipsoidal shape illustrated in Fig. 11 .
  • advantages similar to those of the configurations illustrated in Figs. 7 and 8 can be obtained.
  • the notch 66 or the slit 67 is provided in the heat source side heat exchanger 12a.
  • the present invention is not limited to these configurations.
  • the notch 66 or the slit 67 may be provided in the heat source side heat exchanger 12b. In such a case, advantages similar to those in the configurations illustrated in Figs. 7 , 8 , and 10 can be obtained.
  • Fig. 12 schematically illustrates an example configuration in which part of the fins is shared and two notches are provided in the air-conditioning apparatus 100 of Embodiment 1.
  • the number of notches 66 or slits 67 of the fins in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is not one notch 66 or slit 67 as illustrated in Figs. 7 , 8 , and 10 .
  • two notches 66 may be formed as illustrated in Fig. 12 , or three or more notches 66 may be formed.
  • advantages similar to those illustrated in Figs. 7 , 8 , and 10 can be obtained. That is, if the product of the heat transfer area and the overall heat transfer coefficient between the fins sandwiching the notches 66 is the same, the heat leakage amount can be reduced to the same degree as the configurations illustrated in Figs. 7 , 8 , and 10 .
  • the notch 66 or slit 67 is provided in the lower end of the heat source side heat exchanger 12a.
  • the present invention is not limited to these examples, and the notch 66 or slit 67 may be provided in the upper end of the heat source side heat exchanger 12b. In this case, advantages similar to those illustrated in Figs. 7 , 8 , and 10 can be obtained.
  • Fig. 13 schematically illustrates an example configuration in which heat source side heat exchangers are placed in an outdoor unit and are disposed one above the other with a clearance interposed therebetween in the air-conditioning apparatus 100 of Embodiment 1.
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b are disposed one above the other (in the stage direction).
  • the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a is separated from the uppermost end face of the fin 62 of the heat source side heat exchanger 12b.
  • a clearance 54 is provided between the lowermost end face of the fin 61 of the upper heat source side heat exchanger 12a and the uppermost end face of the fin 62 of the lower heat source side heat exchanger 12b.
  • the clearance 54 constitutes a heat leakage reducing mechanism.
  • the configuration including the clearance 54 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b can obtain advantages similar to those obtained in the configurations illustrated in Figs. 7 to 12 .
  • the heat source side heat exchanger 12a and the heat source side heat exchanger 12b may be disposed in any manner as long as a space is present between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b.
  • a support plate 53 of, for example, a SUS plate or a coated steel plate may be provided at the bottom of the heat source side heat exchanger 12a so as to support the heat source side heat exchanger 12a.
  • the air passage in the clearance 54 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is preferably covered with, for example, a SUS plate or a coated steel plate so as to reduce the detour of wind.
  • the presence of the clearance 54 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b can reduce the heights of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b that can be placed in the casing of the outdoor unit 1.
  • the number of stages of heat exchanger tubes decreases, and thus, the entire heat transfer area of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b decreases.
  • Fig. 14 is a graph for comparing the heat transfer area ratio and a COP, which is an index indicating the degree of performance of an air-conditioning apparatus, in the air-conditioning apparatus 100 of Embodiment 1.
  • the relationship between the heat transfer area ratio and the COP of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is shown in, for example, Fig. 14 .
  • the capacity of the outdoor unit 1 is 10 horse power (28 kW) with a constant airflow rate.
  • the coefficient of performance is a value (efficiency) obtained by diving the heating capacity by the total input power of the outdoor unit 1 and the indoor unit 2.
  • the heat transfer area ratio of the heat source side heat exchanger 12 is about 96.7% or more.
  • the total number of stages of the heat source side heat exchanger 12a and the heat source side heat exchanger 12b is 60
  • the product of the number of stages and the heat transfer area ratio is about 58. That is, in order to reduce the decreasing rate of the COP within 1 % or less, about 58 or more stages of the heat exchangers are needed.
  • the length of the clearance 54 in the stage direction can be obtained by multiplying the difference between the number of stages without the clearance 54 and the number of stages with the clearance 54 by the distance between the centers of the heat exchanger tubes in the stage direction. For example, suppose the distance between the centers of the heat exchanger tubes in the stage direction is about 20 mm, the length of the clearance 54 in the stage direction needs to be about 40 mm or less, which is obtained by a difference of 2 stages between the 60 stages without the clearance 54 and the 58 stages with the clearance 54 by about 20 mm.
  • the length Ls of the clearance 54 in the stage direction can be expressed as Equation (2), where Ac[-] is a heat transfer area ratio, Dd [stages] is the number of stages without the clearance 54, and Ld [mm] is the distance between the centers of the heat exchanger tubes in the stage direction.
  • Equation (3) is obtained as follows: [Equation 2] Ls ⁇ Dd - Ac ⁇ Dd ⁇ Ld [Equation 3] Ls ⁇ 0.033 ⁇ Dd ⁇ Ld
  • the use of the length Ls of the clearance 54 can reduce the decreasing rate of the COP to about 1% or less and reduce the amount of heat leakage between the heat source side heat exchanger 12a and the heat source side heat exchanger 12a.
  • heat leakage between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b can be reduced in the defrosting operation mode.
  • generation of remaining frost and root ice can be reduced in the interface 63 between the adjacent heat source side heat exchangers 12.
  • the defrosting time is reduced and a decrease in heating capacity is reduced, thereby obtaining comfort in the indoor environments.
  • Fig. 15 is a circuit diagram schematically illustrating an example circuit configuration of an air-conditioning apparatus 200 according to Embodiment 2 of the present invention.
  • FIG. 15 a configuration of the air-conditioning apparatus 200 of Embodiment 2 will be described based on the difference from the air-conditioning apparatus 100 of Embodiment 1.
  • a second opening/closing device 31 a that shuts off a refrigerant of a heat source side heat exchanger 12a is disposed between the heat source side heat exchanger 12a and a refrigerant channel switching device 11.
  • a second opening/closing device 31 b that shuts off a refrigerant of a heat source side heat exchanger 12b is disposed between the heat source side heat exchanger 12b and the refrigerant channel switching device 11.
  • An end of a hot gas bypass pipe 5 is connected to a refrigerant pipe 3 between a discharge part of a compressor 10 and the refrigerant channel switching device 11.
  • the other end of the hot gas bypass pipe 5 branches into two, one of which is connected to a refrigerant pipe 3 between the heat source side heat exchanger 12a and the second opening/closing device 31 a and the other is connected to a refrigerant pipe 3 between the heat source side heat exchanger 12b and the second opening/closing device 31 b.
  • the hot gas bypass pipe 5 connected to the heat source side heat exchanger 12a is provided with a first opening/closing device 30a.
  • the hot gas bypass pipe 5 connected to the heat source side heat exchanger 12b is provided with a first opening/closing device 30b.
  • a third opening/closing device 32a whose opening degree is variable is provided in the pipe of the load side expansion device 22 of the heat source side heat exchanger 12a.
  • a third opening/closing device 32b whose opening degree is variable is provided in the pipe of a load side expansion device 22 of the heat source side heat exchanger 12b.
  • the third opening/closing devices 32a and 32b are expansion devices whose opening degrees (the areas of the opening ports) can be changed in order to adjust the internal pressure of the heat source side heat exchanger 12 serving as a condenser.
  • the other part of the configuration is similar to that of the air-conditioning apparatus 100 of Embodiment 1, and thus, description thereof is not repeated.
  • Flows of a refrigerant in the cooling-only operation mode and the heating-only operation mode in the air-conditioning apparatus 200 are similar to those in air-conditioning apparatus 100 of Embodiment 1, and thus, description thereof is not repeated.
  • the first opening/closing device 30a, the first opening/closing device 30b, the second opening/closing device 31 a, the second opening/closing device 31 b, the third opening/closing device 32a, and the third opening/closing device 32b constitute "connection switching devices" of the invention.
  • the lower heat source side heat exchanger 12b in the casing 51 is defrosted, and then the upper heat source side heat exchanger 12a in the casing 51 is defrosted.
  • Conditions for starting the defrosting operation mode are similar to those in the air-conditioning apparatus 100 of Embodiment 1.
  • Fig. 15 the flow direction of a refrigerant in defrosting of the heat source side heat exchanger 12b is indicated by solid arrow lines.
  • the refrigerant channel switching device 11 In the defrosting operation mode, the refrigerant channel switching device 11 is maintained in a state indicated by the solid lines in Fig. 15 .
  • the first opening/closing device 30b is switched to an open state, and allows the refrigerant to pass therethrough.
  • the second opening/closing device 31 b is switched to a closed state, and shuts off the refrigerant.
  • the first opening/closing device 30a is kept in a closed state, and shuts off the refrigerant.
  • the second opening/closing device 31 a is kept in an open state, and allows the refrigerant to pass therethrough.
  • the third opening/closing device 32b is set in a fully open state, and allows the refrigerant to pass therethrough.
  • the opening degree of the third opening/closing device 32a is controlled by the control device 50 such that the saturation pressure of a two-phase refrigerant calculated from the detection result of the sixth temperature sensor 48b is a predetermined value (e.g., about 0.8 MPa in the case of an R410A refrigerant) or more.
  • a predetermined value e.g., about 0.8 MPa in the case of an R410A refrigerant
  • the low-temperature low-pressure refrigerant is compressed and becomes a high-temperature high-pressure gas refrigerant, and the resulting refrigerant is discharged.
  • Part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 is subjected to a pressure reduction in the hot gas bypass pipe 5 and the first opening/closing device 30b such that the temperature of the gas refrigerant is 0 degrees C or more in terms of the saturation temperature.
  • the resulting refrigerant becomes an intermediate-pressure high-temperature gas refrigerant, and flows into the heat source side heat exchanger 12b.
  • the intermediate-pressure high-temperature gas refrigerant that has flowed into the heat source side heat exchanger 12b becomes an intermediate-pressure low-quality two-phase refrigerant or an intermediate-pressure refrigerant while melting frost on the heat source side heat exchanger 12b, and passes through the third opening/closing device 32b.
  • the refrigerant passed through the third opening/closing device 32b merges with the intermediate-pressure low-temperature low-quality two-phase refrigerant or the liquid refrigerant that has flowed into the outdoor unit 1 from the indoor unit 2 upstream of the third opening/closing device 32a.
  • the other part of the high-temperature high-pressure gas refrigerant discharged from the compressor 10 flows out of the outdoor unit 1 through the refrigerant channel switching device 11.
  • the high-temperature high-pressure gas refrigerant that has flowed from the outdoor unit 1 flows into the indoor unit 2 through the refrigerant main pipe 4, transfers heat to the indoor air in the load side heat exchanger 21, and becomes a liquid refrigerant while heating the indoor air.
  • the liquid refrigerant that has flowed from the load side heat exchanger 21 expands in the load side expansion device 22, becomes a low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant, and flows into the outdoor unit 1 again through the refrigerant main pipe 4.
  • the low-temperature intermediate-pressure two-phase refrigerant or liquid refrigerant that has flowed into the outdoor unit 1 merges with the refrigerant from the third opening/closing device 32b upstream of the third opening/closing device 32a, and the merged refrigerant flows into the heat source side heat exchanger 12a.
  • the refrigerant that has flowed into the heat source side heat exchanger 12a absorbs heat from the outdoor air, and becomes a low-temperature low-pressure gas refrigerant.
  • the gas refrigerant that has flowed from the heat source side heat exchanger 12a is sucked into the compressor 10 again through the refrigerant channel switching device 11 and an accumulator 13.
  • the control device 50 controls the opening degree of the third opening/closing device 32a such that the saturation pressure of the two-phase refrigerant calculated from the detection result of the sixth temperature sensor 48b is a predetermined value (e.g., about 0.8 MPa in the case of an R410A refrigerant) or more. That is, the control device 50 controls the opening degree of the third opening/closing device 32a such that the saturation pressure of the two-phase refrigerant calculated from the detection result of the sixth temperature sensor 48b is 0 degrees C or more in terms of the saturation temperature.
  • a predetermined value e.g., about 0.8 MPa in the case of an R410A refrigerant
  • frost is determined to be melt when the temperature of the third temperature sensor 48b reaches a predetermined temperature (e.g., 5 degrees C) or more, for example.
  • the saturation temperature of the refrigerant in the heat source side heat exchanger 12 serving as a condenser is set at an intermediate pressure (e.g., about 0.8 MPa or more in the case of an R410A refrigerant), which is higher than the frost temperature, that is, higher than 0 degrees C.
  • an intermediate pressure e.g., about 0.8 MPa or more in the case of an R410A refrigerant
  • the two-phase range (latent heat) of the refrigerant can be used, and substantially the same degrees of defrosting capacity can be obtained with an amount of refrigerant circulation smaller than that in the configuration of the air-conditioning apparatus 100 of Embodiment 1.
  • the heat leakage reducing mechanism is configured such that fins are not shared but are separated in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b as illustrated in Fig. 7 .
  • the saturation temperature T1 of a two-phase refrigerant flowing in a condenser that performs defrosting is 5 degrees C
  • the temperature T2 of a refrigerant flowing in an evaporator that performs heating operation is -25 degrees C.
  • the inter-fin distance ⁇ between an end of the heat transmission pipe of the evaporator and an end of the heat transmission pipe of the condenser in the interface 63 is 12.5 mm, and in a state where the heat exchangers are not separated, the fin width is 17 mm, the fin thickness is 0.1 mm, and the number of fins is 3700.
  • the heat leakage amount Q1 from the condenser to the evaporator in a case where the fins are separated and are shared is about 3.22 kW from Equation (1).
  • the overall heat transfer coefficient is a half of the product of a heat transfer area (a contact area) and the overall heat transfer coefficient in a case where the fins are shared.
  • the heat leakage amount Q1 from the condenser to the evaporator by thermal conduction of the fins is reduced as compared to the case where all the fins are shared by about 25% or more, and the heat leakage amount Q1 is about 2.42 kW.
  • the quantity of heat Q2 (calculated by multiplying latent heat of melting frost and the weight of frost) necessary for melting frost accumulated on the evaporator is about 1.5 MJ
  • the heat exchange amount Q3 between frost and a refrigerant used in defrosting in a case where no heat leakage amount is present from the condenser to the evaporator by thermal conduction of the fins is about 5.5 kW.
  • the time required for completion of defrosting is obtained by subtracting the difference between the heat exchange amount Q3 and the heat leakage amount Q1 from the solution heat amount Q2 of frost.
  • the heat leakage amount Q1 is reduced by about 25% to be about 2.42 kW, and suppose the heat exchange amounts Q2 and Q3 are under the above conditions, the time required for completion of defrosting is about 8 minutes.
  • the time required for completion of defrosting can be reduced by about 3 minutes.
  • the reduction of the time required for completion of defrosting enables part of a refrigerant discharged from the compressor 10 for defrosting to be quickly used for heating, as compared to a case where heat leakage occurs from the condenser to the evaporator by thermal conduction of the fins.
  • a decrease in heating capacity can be reduced.
  • a temperature decrease in the room can be reduced, thereby obtaining comfort in the indoor environments.
  • a temperature decrease is reduced in the fin at the condenser side in the interface 63 between the heat source side heat exchanger 12a and the heat source side heat exchanger 12b, and thus, adfreezing of water drops generated by defrosting of the upper heat exchanger serving as the condenser can be reduced, thereby reducing generation of root ice.
  • the air-conditioning apparatus 200 of Embodiment 2 employs the configuration illustrated in Fig. 7 as a configuration of the heat leakage reducing mechanism, but the present invention is not limited to this configuration.
  • the configuration of the heat leakage reducing mechanism may be any one of the configurations illustrated in Figs. 8 to 13 described in Embodiment 1. In such cases, similar advantages as those obtained in the configuration illustrated in Fig. 7 can be obtained.
  • the two devices that is, the third opening/closing device 32a and the third opening/closing device 32b, are expansion devices whose opening degrees (areas of opening ports) are variable, but the present invention is not limited to this example.
  • the third opening/closing device 32b (or the third opening/closing device 32a) may be changed to a expansion device whose opening degree (the area of the opening port) is variable.
  • the unchanged third opening/closing device 32a (or the third opening/closing device 32b) is always open, and the third opening/closing device 32b (or the third opening/closing device 32a) changed to the expansion device whose opening degree (the area of the opening port) is variable is used.
  • the internal pressure of the heat source side heat exchanger 12 serving as a condenser is adjusted. In this state, an operation similar to that of the air-conditioning apparatus 200 illustrated in Fig. 15 can be performed, and similar advantages can be obtained.
  • the saturation temperature of a refrigerant in the heat source side heat exchanger 12 serving as a condenser can be set at a temperature corresponding to an intermediate pressure (e.g., about 0.8 MPa or more in the case of an R410A refrigerant) higher than the frost temperature, that is, higher than 0 degrees C, in the defrosting operation.
  • an intermediate pressure e.g., about 0.8 MPa or more in the case of an R410A refrigerant
  • the number of second opening/closing devices 31 that are expansion devices whose opening degrees (the areas of the opening ports) can be changed may be one.
  • Such a configuration can reduce the number of expansion devices whose opening degrees (the areas of the opening ports), such as electronic expansion valves including stepping motors, generally having structures more complicated and expensive than solenoid valves, and thus, the outdoor unit 1 can be fabricated at low cost.
  • the third opening/closing device 32b (or the third opening/closing device 32a) may be changed to a expansion device whose opening degree (the area of the opening port) is variable.
  • the third opening/closing device 32 is provided, and the internal pressure of the heat source side heat exchanger 12 serving as a condenser is adjusted in the defrosting operation.
  • an operation similar to that of the air-conditioning apparatus 200 illustrated in Fig. 15 can be performed, and similar advantages can be obtained.
  • the configuration illustrated in Fig. 17 can simplify the circuit configuration, and thus, the outdoor unit 1 can be fabricated at low cost.
  • the third opening/closing device 32b (or the third opening/closing device 32a) may be changed to a expansion device whose opening degree (the area of the opening port) is variable, and this third opening/closing device 32 is provided.
  • a fourth opening/closing device 33a and a fourth opening/closing device 33b for shutting off the refrigerant in the heat source side heat exchanger 12a or the heat source side heat exchanger 12b are disposed in refrigerant pipes 3 connecting the heat source side heat exchanger 12a and the heat source side heat exchanger 12b to the third opening/closing device 32b (or the third opening/closing device 32a).
  • a refrigerant bypass pipe 6 is provided. An end of the refrigerant bypass pipe 6 is connected to the refrigerant pipes 3 connecting the heat source side heat exchangers 12a and 12b to the fourth opening/closing devices 33, and the other end of the refrigerant bypass pipe 6 is connected to the channel between the third opening/closing device 32 and the load side expansion device 22.
  • the refrigerant bypass pipe 6 allows the refrigerant in the heat source side heat exchanger 12 serving as a condenser in the defrosting operation mode to flow in the refrigerant pipes 3.
  • a fifth opening/closing device 34a and a fifth opening/closing device 34b for switching a refrigerant channel of the refrigerant bypass pipe 6 is provided in the refrigerant bypass pipe 6 between the heat source side heat exchanger 12 and the fourth opening/closing device 33 whose one ends correspond to each other.
  • the fourth opening/closing device 33a is an open state.
  • the fourth opening/closing device 33b is a closed state.
  • the fifth opening/closing device 34a is in a closed state.
  • the fifth opening/closing device 34b is in an open state.
  • the internal pressure of the heat source side heat exchanger 12b serving as a condenser is adjusted by the third opening/closing device 32b (of the third opening/closing device 32a). Part of condensed refrigerant merges with another refrigerant flowing out of the load side expansion device 22 into the outdoor unit 1 in the refrigerant pipes 3 between the third opening/closing device 32b (or the third opening/closing device 32a) and the load side expansion device 22 through the fifth opening/closing device 34b.
  • all the refrigerant absorbs heat from the air in the heat source side heat exchanger 12a serving as an evaporator through the third opening/closing device 32b (or the third opening/closing device 32a) and the fourth opening/closing device 33a, becomes a low-pressure two-phase or gas refrigerant, and then is sucked into the compressor 10 through the second opening/closing device 31 a, the refrigerant channel switching device 11, and the accumulator 13.
  • the open/closed states of the first opening/closing devices 30a and 30b, the fourth opening/closing devices 33a and 33b, and the fifth opening/closing devices 34a and 34b are reversed, and the flow of the refrigerant in the heat source side heat exchanger 12a is replaced by the flow of the refrigerant in the heat source side heat exchanger 12b.
  • the heat source side refrigerant of each of Embodiment 1 and Embodiment 2 may be a nonflammable refrigerant such as R410A, R407C, and R22, HFO1234yf, HFO1234ze(E), R32, HC, a mixed refrigerant including R32 and HFO1234yf, a slightly flammable refrigerant such as a refrigerant using a mixed refrigerant including at least one of the previously listed refrigerants, a highly flammable refrigerant such as propane (R290), and a refrigerant such as CO2(R744) operating in a supercritical state under high pressures.
  • a nonflammable refrigerant such as R410A, R407C, and R22, HFO1234yf, HFO1234ze(E), R32, HC, a mixed refrigerant including R32 and HFO1234yf, a slightly flammable refrigerant such as a refrigerant using
  • the first opening/closing devices 30a and 30b are solenoid valves.
  • valves whose opening degrees are variable such as electronic expansion valves, may be used as shut-off valves, as well as the solenoid valves.
  • the second opening/closing devices 31 a and 31 b are solenoid valves.
  • valves whose opening degrees are variable such as electronic expansion valves, may be used as shut-off valves, as well as the solenoid valves.
  • the third opening/closing devices 32a and 32b are expansion devices whose opening degrees (the areas of the opening ports) are variable, but any devices may be used as long as the area of the opening port of the channel can be changed.
  • the expansion devices may be electronic expansion valves driven by stepping motors, or a plurality of small solenoid valves may be arranged in parallel so that the area of the opening port can be changed by switching the solenoid valves.
  • the fourth opening/closing device 33 of Embodiment 2 is a solenoid valve as an example.
  • valves whose opening degrees are variable such as electronic expansion valves, may be used as shut-off valves, as well as the solenoid valves.
  • the fifth opening/closing device 34 of Embodiment 2 is a solenoid valve as an example.
  • valves whose opening degrees are variable such as electronic expansion valves, may be used as shut-off valves, as well as the solenoid valves.
  • the heat source side heat exchangers 12a and 12b of Embodiment 1 and Embodiment 2 are bent in U shapes, and are stacked in two stages in a stage direction (i.e., vertically such that the fins thereof are oriented in the same direction).
  • stage direction i.e., vertically such that the fins thereof are oriented in the same direction.
  • the present invention is not limited to this configuration.
  • the heat source side heat exchangers 12 may be straight and stacked in three stages in the stage direction (i.e., vertically such that the fins thereof are oriented in the same direction).
  • the heat source side heat exchangers 12 do not need to be disposed one above the other vertically, and may be disposed side by side or laterally or longitudinally.
  • Each of the air-conditioning apparatus 100 of Embodiment 1 and the air-conditioning apparatus 200 of Embodiment 2 is an air-conditioning apparatus that switches between a cooling operation and a heating operation, as an example.
  • the present invention is not limited to this type, and is applicable to an air-conditioning apparatus having a circuit configuration that can perform a cooling operation and a heating operation at the same time.
  • the refrigerant channel switching device 11 may be omitted so that only the heating-only operation mode and the defrosting operation mode are performed.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Air Conditioning Control Device (AREA)
EP12889228.8A 2012-11-29 2012-11-29 Dispositif de conditionnement de l'air Active EP2930450B1 (fr)

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CN107504746A (zh) * 2017-08-22 2017-12-22 广东美的暖通设备有限公司 热泵组件、除霜控制方法和存储介质
US10508826B2 (en) 2015-01-13 2019-12-17 Mitsubishi Electric Corporation Refrigeration cycle apparatus
US10520233B2 (en) 2015-01-13 2019-12-31 Mitsubishi Electric Corporation Air-conditioning apparatus for a plurality of parallel outdoor units
EP3604975A4 (fr) * 2017-03-27 2020-03-25 Daikin Industries, Ltd. Unité d'échangeur de chaleur
US11415371B2 (en) 2017-03-27 2022-08-16 Daikin Industries, Ltd. Heat exchanger and refrigeration apparatus

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WO2020079835A1 (fr) * 2018-10-19 2020-04-23 三菱電機株式会社 Climatiseur
CN114061030A (zh) * 2021-10-28 2022-02-18 青岛海尔空调器有限总公司 一种空调除霜控制方法、控制装置及空调器

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JP4675927B2 (ja) * 2007-03-30 2011-04-27 三菱電機株式会社 空気調和装置
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US10508826B2 (en) 2015-01-13 2019-12-17 Mitsubishi Electric Corporation Refrigeration cycle apparatus
US10520233B2 (en) 2015-01-13 2019-12-31 Mitsubishi Electric Corporation Air-conditioning apparatus for a plurality of parallel outdoor units
CN106225294A (zh) * 2016-08-29 2016-12-14 烟台欧森纳地源空调股份有限公司 一种低温风冷热泵系统
EP3604975A4 (fr) * 2017-03-27 2020-03-25 Daikin Industries, Ltd. Unité d'échangeur de chaleur
US11415371B2 (en) 2017-03-27 2022-08-16 Daikin Industries, Ltd. Heat exchanger and refrigeration apparatus
US11428446B2 (en) 2017-03-27 2022-08-30 Daikin Industries, Ltd. Heat exchanger unit
CN107504746A (zh) * 2017-08-22 2017-12-22 广东美的暖通设备有限公司 热泵组件、除霜控制方法和存储介质

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JP5980349B2 (ja) 2016-08-31

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