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WO2022168305A1 - Air-conditioning device - Google Patents

Air-conditioning device Download PDF

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Publication number
WO2022168305A1
WO2022168305A1 PCT/JP2021/004555 JP2021004555W WO2022168305A1 WO 2022168305 A1 WO2022168305 A1 WO 2022168305A1 JP 2021004555 W JP2021004555 W JP 2021004555W WO 2022168305 A1 WO2022168305 A1 WO 2022168305A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanger
air
refrigerant
operation mode
temperature
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.)
Ceased
Application number
PCT/JP2021/004555
Other languages
French (fr)
Japanese (ja)
Inventor
淳 西尾
皓亮 宮脇
宗史 池田
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
Original Assignee
Mitsubishi Electric Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP2021541261A priority Critical patent/JP6980165B1/en
Priority to PCT/JP2021/004555 priority patent/WO2022168305A1/en
Publication of WO2022168305A1 publication Critical patent/WO2022168305A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/70Control systems characterised by their outputs; Constructional details thereof
    • F24F11/80Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air
    • F24F11/86Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling compressors within refrigeration or heat pump circuits
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification

Definitions

  • the present disclosure relates to an air conditioner having a dehumidifying operation mode and a cooling operation mode.
  • a heat pump circuit that uses a heat exchanger to recover heat from return air returning from the room to the outside.
  • high-temperature and high-pressure gas refrigerant discharged from the compressor mounted on the outdoor unit flows into the heat exchanger mounted on the indoor unit. Since the heat exchanger functions as a condenser, the inflow refrigerant is condensed in the heat exchanger to become liquid refrigerant. After that, the liquid refrigerant is depressurized by the expansion valve, and becomes a gas-liquid two-phase state in which gas refrigerant and liquid refrigerant are mixed.
  • the gas-liquid two-phase refrigerant flows into a heat exchanger mounted on the outdoor unit and functioning as an evaporator.
  • the liquid refrigerant of the gas-liquid two-phase refrigerant is evaporated to become a low-pressure gas refrigerant.
  • the gas refrigerant sent out from the heat exchanger flows into the compressor, is compressed by the compressor, becomes high-temperature and high-pressure gas refrigerant, and is discharged from the compressor again. This cycle is then repeated.
  • the outside air conditioner takes in outside air from the outside with a fan, cools or heats it with a heat exchanger, and supplies it to the room. Also, the outdoor air conditioner takes in return air from the room, cools or heats it with a heat exchanger, and exhausts it to the outside.
  • outdoor air conditioner adjusts the temperature and humidity of the outdoor air so that the temperature and humidity of the outdoor air are close to those of the indoor air, thereby supplying comfortable and hygienic air to the user.
  • outdoor air conditioners with multiple operation modes such as an operation mode that cools and dehumidifies according to the difference in temperature and humidity between indoors and outdoors, and an operation mode that only dehumidifies and maintains a constant temperature, are known. It is
  • the ventilation air conditioner described in Patent Document 1 is an air conditioner that has such an outside air conditioner function.
  • the air conditioner described in Patent Document 1 has a refrigerant circuit in which the circulation direction of the refrigerant can be switched by operating a four-way valve and a solenoid valve in order to achieve both temperature control and humidity control, and an air circulation path.
  • a plurality of operation modes are realized by using a switching device for switching.
  • An object of the present invention is to provide an air conditioner capable of supplying comfortable air to a user by suppressing fluctuations in supply air temperature.
  • An air conditioner includes an air supply fan and an air supply path for supplying outdoor air to a room, a return air fan and a return air path for returning the indoor air to the outdoor, a compressor, A heat pump circuit in which a first heat exchanger, a second heat exchanger, a throttle device, and a third heat exchanger are connected in this order by refrigerant piping, the supply air fan, the return air fan, and the heat pump circuit. and a control unit that controls operation, wherein the first heat exchanger is arranged in the return air path, and the refrigerant and the return air flowing inside the first heat exchanger are arranged in the return air path.
  • the second heat exchanger and the third heat exchanger are arranged in the air supply path, and the second heat exchanger and the third heat exchanger are arranged in the air supply path, respectively.
  • Heat is exchanged between the refrigerant flowing inside the heat exchanger and the air flowing inside the air supply path, and the air conditioner has two operation modes, one for cooling the room and one for dehumidifying the room.
  • the refrigerant discharged from the compressor flows into the first heat exchanger, and the refrigerant flowing out of the third heat exchanger is Refrigerant flows through the refrigerant pipe in the direction of being sucked into the compressor, and in the cooling operation mode, the first heat exchanger acts as a condenser, and the second heat exchanger and the third heat exchanger acts as an evaporator, and in the dehumidifying operation mode, the first heat exchanger and the second heat exchanger act as condensers, and the third heat exchanger acts as an evaporator.
  • the air conditioner according to the present disclosure it is possible to continuously switch between the dehumidifying operation mode and the cooling operation mode with a simple configuration that does not require switching of the refrigerant flow path when switching between the cooling operation and the dehumidifying operation. can. As a result, fluctuations in the supply air temperature can be suppressed, and user comfort can be improved.
  • FIG. 1 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200 according to Embodiment 1.
  • FIG. FIG. 4 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1; 4 is a Mollier diagram showing refrigerant states in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 4 is a flowchart showing the operation of the control unit 90 in the cooling operation mode of the air conditioner 200 according to Embodiment 1.
  • FIG. 4 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1; 4 is a Mollier diagram showing refrigerant states in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 4 is a flow chart showing the operation of the control unit 90 in the dehumidifying operation mode in the air conditioner 200 according to Embodiment 1.
  • FIG. 4 is an explanatory diagram showing operation mode switching operation based on the opening degree OP of the expansion device 17 in the air conditioner 200 according to Embodiment 1.
  • FIG. 4 is a flowchart showing operation mode switching operation of the control unit 90 in the air conditioner 200 according to Embodiment 1.
  • FIG. 2 is a side view showing the configuration of heat transfer tubes of first heat exchanger 11 and second heat exchanger 12 in air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 2 is a plan view illustrating an example of the arrangement of second heat exchanger 12 and third heat exchanger 13 in air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 4 is a side view illustrating a modification of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1.
  • FIG. FIG. 7 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200B according to Embodiment 2; 9 is a flow chart showing the operation of the control unit 90 in the air conditioner 200B according to Embodiment 2.
  • FIG. 11 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3; 2 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1.
  • FIG. 11 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3; 2 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1.
  • FIG. 11 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3; 2 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1.
  • FIG. 11 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3; 2 is
  • FIG. 1 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200 according to Embodiment 1.
  • the air conditioner 200 functions as an outdoor air conditioner that ventilates a room, for example.
  • the air conditioner 200 has a cooling operation mode and a dehumidification operation mode as operation modes.
  • the air conditioner 200 is installed, for example, at the boundary between an indoor space 300 and an outdoor space 301 .
  • a room 300 is a space to be air-conditioned by the air conditioner 200 .
  • the air conditioner 200 may be installed indoors 300 .
  • the air conditioner 200 includes a heat pump circuit including a compressor 16, an expansion device 17, a first heat exchanger 11, a second heat exchanger 12, and a third heat exchanger 13.
  • Compressor 16, first heat exchanger 11, second heat exchanger 12, expansion device 17, and third heat exchanger 13 are connected by refrigerant pipe 18 to form a refrigerant circuit.
  • the refrigerant flows in the same direction in the cooling operation mode and the dehumidifying operation mode. Specifically, in the cooling operation mode and the dehumidifying operation mode, the refrigerant is flow in order.
  • the air conditioner 200 includes an air supply path 19 and an air supply fan 14 for supplying air from the outdoor 301 to the indoor 300 .
  • the air supply fan 14 is arranged in the air supply path 19 .
  • the air conditioner 200 also includes a return air path 20 and a return air fan 15 for returning the air in the room 300 to the outside 301 .
  • the return air fan 15 is arranged in the return air path 20 .
  • the four arrows in FIG. 1 respectively indicate the ventilation directions of the outside air OA, the supply air SA, the return air RA, and the exhaust air EA.
  • the outside air OA is air supplied from the outdoor 301 to the second heat exchanger 12 and the third heat exchanger 13 by the air supply fan 14, and flows in the air supply path 19 in the direction from the outdoor 301 to the indoor 300.
  • the supply air SA is the air supplied from the second heat exchanger 12 and the third heat exchanger 13 to the room 300 by the supply fan 14, and is directed in the air supply path 19 from the outdoor 301 to the indoor 300.
  • the return air RA is air supplied from the room 300 to the first heat exchanger 11 by the return air fan 15 and flows in the return air path 20 in the direction from the room 300 to the outside 301 .
  • the exhaust EA is air that is discharged from the first heat exchanger 11 to the outdoor 301 by the return air fan 15 , and flows in the return air path 20 in the direction from the indoor 300 to the outdoor 301 .
  • the air supply path 19 is an air path that connects the outdoor 301 and the indoor 300 .
  • the air supply path 19 is composed of, for example, a duct.
  • the air supply fan 14 is provided in the air supply path 19 and blows air from the outdoor 301 to the indoor 300 .
  • the air supply fan 14 supplies the outside air OA to the second heat exchanger 12 and the third heat exchanger 13 .
  • the return air path 20 is an air path that connects the indoor 300 and the outdoor 301 .
  • the return air path 20 is composed of, for example, a duct.
  • the return air fan 15 is provided in the return air path 20 and blows air from the indoor 300 to the outdoor 301 .
  • the return air fan 15 supplies the return air RA to the first heat exchanger 11 .
  • the form of the supply air fan 14 and the return air fan 15 may be any of a centrifugal fan, an axial flow fan, and a cross flow fan. may be Also, the air supply fan 14 may be located upstream or downstream of the second heat exchanger 12 and the third heat exchanger 13 . Similarly, the return air fan 15 may be upstream or downstream of the first heat exchanger 11 .
  • the compressor 16 has a suction port and a discharge port.
  • the compressor 16 sucks the refrigerant through the suction port, compresses the refrigerant, and discharges the compressed refrigerant through the discharge port.
  • the compressor 16 can be configured by, for example, a rotary compressor, a scroll compressor, a screw compressor, or a reciprocating compressor.
  • the operating frequency may be arbitrarily changed by an inverter circuit or the like to change the refrigerant delivery capacity of the compressor 16 per unit time. In that case, the operating frequency of the compressor 16 is controlled by the controller 90, which will be described later.
  • the first heat exchanger 11 is connected to the discharge port of the compressor 16 via refrigerant piping 18 . High-temperature, high-pressure refrigerant discharged from the compressor 16 flows into the first heat exchanger 11 . As shown in FIG. 1 , the first heat exchanger 11 is arranged within the return air path 20 . The first heat exchanger 11 has therein heat transfer tubes through which a refrigerant flows. The first heat exchanger 11 is, for example, a fin-and-tube heat exchanger. The first heat exchanger 11 exchanges heat between the refrigerant flowing through the heat transfer tubes and the return air RA. The first heat exchanger 11 functions as a condenser in the cooling operation mode and the dehumidifying operation mode.
  • the second heat exchanger 12 is arranged downstream of the first heat exchanger 11 in the direction of refrigerant flow in the cooling operation mode.
  • the refrigerant discharged from the first heat exchanger 11 flows into the second heat exchanger 12 .
  • the second heat exchanger 12 is arranged in the air supply path 19 .
  • the second heat exchanger 12 has therein heat transfer tubes through which a refrigerant flows.
  • the second heat exchanger 12 is, for example, a fin-and-tube heat exchanger.
  • the second heat exchanger 12 exchanges heat between the refrigerant flowing through the heat transfer tubes and the outside air OA.
  • the second heat exchanger 12 functions as an evaporator in the cooling operation mode, and functions as a condenser in the dehumidification operation mode.
  • the third heat exchanger 13 is arranged downstream of the second heat exchanger 12 in the direction of refrigerant flow in the cooling operation mode.
  • the refrigerant discharged from the second heat exchanger 12 flows into the third heat exchanger 13 via the expansion device 17 .
  • the third heat exchanger 13 is arranged in the air supply path 19 .
  • the third heat exchanger 13 has therein heat transfer tubes through which a refrigerant flows.
  • the third heat exchanger 13 is, for example, a fin-and-tube heat exchanger.
  • the third heat exchanger 13 exchanges heat between the refrigerant flowing through the heat transfer tubes and the outside air OA.
  • the third heat exchanger 13 functions as an evaporator in the cooling operation mode and the dehumidifying operation mode.
  • the expansion device 17 is arranged between the second heat exchanger 12 and the third heat exchanger 13 .
  • the expansion device 17 expands and decompresses the refrigerant that has passed through the first heat exchanger 11 and the second heat exchanger 12 .
  • the throttle device 17 can be composed of, for example, an electric expansion valve capable of adjusting the flow rate of the refrigerant.
  • the air conditioner 200 has a plurality of detectors 80-88.
  • the detection results of the detection units 80 to 88 are input to the control unit 90 . These detection units 80 to 88 will be described below.
  • the first temperature/humidity detector 80 is arranged in the air supply path 19 .
  • the first temperature/humidity detector 80 is arranged downstream of the second heat exchanger 12 and the third heat exchanger 13 in the direction of air flow.
  • the first temperature/humidity detector 80 detects the temperature and humidity of the supplied air SA.
  • the first temperature/humidity detector 80 is composed of, for example, a temperature sensor and a humidity sensor.
  • the second temperature/humidity detection unit 81 is arranged in the return air path 20 .
  • the second temperature/humidity detector 81 is arranged upstream of the first heat exchanger 11 in the direction of air flow.
  • the second temperature/humidity detector 81 detects the temperature and humidity of the return air RA.
  • the second temperature/humidity detector 81 is composed of, for example, a temperature sensor and a humidity sensor.
  • the outside air temperature detector 82 is arranged inside the air supply path 19 .
  • the outside air temperature detector 82 is arranged upstream of the second heat exchanger 12 and the third heat exchanger 13 in the direction of air flow.
  • the outside air temperature detector 82 detects the temperature of the outside air OA.
  • the outside air temperature detector 82 is composed of, for example, a temperature sensor.
  • the first refrigerant temperature detector 83 is attached to the refrigerant pipe 18 between the first heat exchanger 11 and the second heat exchanger 12 .
  • the first refrigerant temperature detector 83 is arranged downstream of the first heat exchanger 11 in the direction of refrigerant flow in the cooling operation mode.
  • the first refrigerant temperature detector 83 detects the outlet refrigerant temperature of the first heat exchanger 11 .
  • the first coolant temperature detection unit 83 is composed of, for example, a temperature sensor.
  • the second refrigerant temperature detector 84 is attached to the refrigerant pipe 18 between the second heat exchanger 12 and the third heat exchanger 13 .
  • the second refrigerant temperature detector 84 is arranged, for example, downstream of the second heat exchanger 12 and upstream of the expansion device 17 in the direction of refrigerant flow in the cooling operation mode.
  • the second refrigerant temperature detector 84 detects the outlet refrigerant temperature of the second heat exchanger 12 .
  • the second coolant temperature detection unit 84 is composed of, for example, a temperature sensor.
  • the third refrigerant temperature detector 85 is attached to the refrigerant pipe 18 between the third heat exchanger 13 and the compressor 16 .
  • the third refrigerant temperature detector 85 is arranged downstream of the third heat exchanger 13 in the direction of refrigerant flow in the cooling operation mode.
  • the third refrigerant temperature detector 85 detects the outlet refrigerant temperature of the third heat exchanger 13 .
  • the third coolant temperature detection unit 85 is composed of, for example, a temperature sensor.
  • the discharge pressure detector 86 is arranged on the discharge port side of the compressor 16 .
  • the discharge pressure detector 86 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the first heat exchanger 11 .
  • a discharge pressure detector 86 detects the pressure of the refrigerant discharged from the compressor 16 .
  • the discharge pressure detection unit 86 is composed of, for example, a pressure sensor.
  • the suction pressure detector 87 is arranged on the suction port side of the compressor 16 .
  • the suction pressure detector 87 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the third heat exchanger 13 .
  • the suction pressure detector 87 detects the pressure of the refrigerant sucked into the compressor 16 .
  • the suction pressure detection unit 87 is composed of, for example, a pressure sensor.
  • the discharge temperature detector 88 is arranged on the discharge port side of the compressor 16 .
  • the discharge temperature detector 88 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the first heat exchanger 11 .
  • a discharge temperature detector 88 detects the temperature of the refrigerant discharged from the compressor 16 .
  • the discharge temperature detection unit 88 is composed of, for example, a temperature sensor.
  • FIG. 1 shows the refrigerant circuit configuration when the air conditioner 200 performs only the cooling operation and the dehumidifying operation
  • the air conditioner 200 is not limited to that case, and the air conditioner 200 may also perform the heating operation.
  • FIG. 16 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1. As shown in FIG.
  • the air conditioner 200A has a cooling operation mode, a dehumidifying operation mode, and a heating operation mode.
  • a channel switching device 30, a second expansion device 31, and a fourth refrigerant temperature detection section 89 are added to the configuration of FIG.
  • the flow switching device 30 is arranged between the discharge port of the compressor 16 and the first heat exchanger 11 and the third heat exchanger 13 .
  • the channel switching device 30 is composed of, for example, a four-way valve.
  • the flow path switching device 30 switches the direction of refrigerant flow depending on whether the operation mode of the air conditioner 200 is the cooling operation mode or the heating operation mode. However, also in the air conditioner 200A, as in the air conditioner 200, the direction in which the refrigerant flows is the same between the cooling operation mode and the dehumidifying operation mode. 16, the solid line of the flow switching device 30 indicates the state of the flow switching device 30 in the cooling operation mode, and the broken line of the flow switching device 30 indicates the state of the flow switching device 30 in the heating operation mode. showing.
  • the flow switching device 30 connects the discharge port of the compressor 16 and the first heat exchanger 11 and connects the suction port of the compressor 16 and the third heat exchanger 13. Switch refrigerant flow to connect.
  • the flow switching device 30 connects the discharge port of the compressor 16 and the third heat exchanger 13, and connects the suction port of the compressor 16 and the first heat exchanger 11. Switch refrigerant flow to connect. As a result, the direction in which the refrigerant flows is reversed between the cooling operation mode and the heating operation mode.
  • the refrigerant discharged from the compressor 16 flows into the first heat exchanger 11 via the flow switching device 30 . That is, in the cooling operation mode, the refrigerant is the compressor 16, the flow path switching device 30, the first heat exchanger 11, the second expansion device 31, the second heat exchanger 12, the expansion device 17, the third heat exchanger 13, the flow switching device 30, and the compressor 16 in this order.
  • the refrigerant discharged from the compressor 16 flows through the flow path switching device 30 into the third heat exchanger 13 . That is, in the heating operation mode, the refrigerant is the compressor 16, the flow path switching device 30, the third heat exchanger 13, the expansion device 17, the second heat exchanger 12, the second expansion device 31, the first heat exchanger 11, the flow switching device 30, and the compressor 16 in this order.
  • the second throttle device 31 is arranged between the first heat exchanger 11 and the second heat exchanger 12 .
  • the second expansion device 31 expands the refrigerant discharged from the second heat exchanger 12 to reduce the pressure.
  • the fourth refrigerant temperature detector 89 is arranged downstream of the first heat exchanger 11 in the refrigerant flow direction in the heating operation mode.
  • the fourth refrigerant temperature detector 89 is provided, for example, in the refrigerant pipe 18 between the first heat exchanger 11 and the flow path switching device 30 .
  • the fourth refrigerant temperature detector 89 detects the outlet refrigerant temperature of the first heat exchanger 11 in the heating operation mode.
  • a detection result of the fourth coolant temperature detection unit 89 is input to the control unit 90 .
  • the flow switching device 30 is added to enable the formation of a refrigerant flow in the direction opposite to that in the cooling operation mode, and the first heat exchanger 11 and the second heat exchanger 12, the air conditioner 200 can perform heating operation.
  • heating operation may be performed by switching the air flow direction. That is, the switching mechanism for switching the air passages so that the first heat exchanger 11 is in the air supply passage 19 and the second heat exchanger 12 and the third heat exchanger 13 are in the return air passage 20, It may be added to the configuration of FIG.
  • control unit 90 As shown in FIG. 1 , the air conditioner 200 further includes a controller 90 .
  • the control unit 90 controls the overall operation of the air conditioner 200, and is composed of, for example, an analog circuit, a digital circuit, a CPU, or a processing circuit in which two or more of these are combined. .
  • the processing circuit is a CPU (processor)
  • each function of that part of the control unit 90 is implemented by software, firmware, or a combination of software and firmware.
  • Software and firmware are written as programs and stored in memory.
  • the processing circuit implements each function of the control unit 90 by reading and executing the program stored in the memory.
  • the memory means, for example, non-volatile or volatile semiconductor memory such as RAM (Random Access Memory), ROM (Read Only Memory), flash memory, EPROM (Erasable Programmable ROM), magnetic disk, flexible disk, optical disk , compact discs, mini discs, and DVDs (Digital Versatile Discs).
  • RAM Random Access Memory
  • ROM Read Only Memory
  • EPROM Erasable Programmable ROM
  • magnetic disk flexible disk
  • optical disk compact discs
  • mini discs mini discs
  • DVDs Digital Versatile Discs
  • control unit 90 controls the operation of the heat pump circuit such as the frequency of the compressor 16 and the opening of the expansion device 17, and the rotation speed of the supply fan 14 and return air. It controls the air flow such as the number of revolutions of the fan 15 .
  • the detection results of the detection units 80 to 88 are, for example, the above-described discharge pressure detection unit 86, suction pressure detection unit 87, discharge temperature detection unit 88, first refrigerant temperature detection unit 83, second refrigerant temperature detection unit 84, and at least one of the detection results of the third refrigerant temperature detection unit 85, the first temperature/humidity detection unit 80, the second temperature/humidity detection unit 81, and the outside air temperature detection unit 82.
  • control unit 90 controls the frequency of the compressor 16, the number of rotations of the supply air fan 14, the number of rotations of the return air fan 15, the opening of the expansion device 17, etc. based on instructions from a remote controller (not shown). to control.
  • the air conditioner 200 is operated in the cooling operation mode or the dehumidifying operation mode.
  • Embodiment 1 shows the case where the control unit 90 is provided inside the air conditioner 200 , the control unit 90 may be provided outside the air conditioner 200 . Further, the control unit 90 may be composed of one control unit, or may be composed of a plurality of control units. When the control unit 90 is composed of a plurality of control units, at least one of them controls the air flow of the supply air fan 14 and the return air fan 15, and at least one of the other controls the refrigerant flow of the heat pump circuit. may be controlled.
  • the second heat exchanger 12 functions as an evaporator in the cooling operation mode, and functions as a condenser in the dehumidification operation mode.
  • the opening degree OP of the expansion device 17 in the cooling operation mode is smaller than that in the dehumidification operation mode.
  • the controller 90 reduces the opening degree OP of the expansion device 17 to reduce the heating capacity of the second heat exchanger 12 for the outside air OA. Further, by increasing the opening degree OP of the expansion device 17, control is performed to increase the heating capacity of the second heat exchanger 12 for the outside air OA.
  • the air conditioner 200 does not need to switch the direction of refrigerant flow between the cooling operation mode and the dehumidifying operation mode due to the above (1) and (2).
  • the controller 90 adjusts the opening degree OP of the expansion device 17 to determine whether the second heat exchanger 12 functions as an evaporator or a condenser. Therefore, it is possible to continuously transition between the dehumidifying operation mode and the cooling operation mode. Further, according to (3) above, the control unit 90 adjusts the opening degree OP of the expansion device 17, so that the heating capacity of the second heat exchanger 12 can be adjusted. As a result, in the operation in the dehumidifying operation mode, the dehumidifying operation that reduces the humidity in the room 300 while suppressing the temperature drop in the room 300 becomes possible. Details will be described below.
  • FIG. 2 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 3 is a Mollier diagram showing refrigerant states in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 3 solid line arrows indicate the direction in which the refrigerant flows, dashed line arrows indicate the direction in which air flows, and examples of temperatures of the refrigerant and air under typical conditions are appended to the arrows.
  • the horizontal axis indicates the enthalpy of the refrigerant
  • the vertical axis indicates the pressure of the refrigerant.
  • FIG. 3 shows air temperature, refrigerant pressure, enthalpy, and refrigerant temperature.
  • the saturated vapor line 40 and the saturated liquid line 41 are indicated by dashed curves.
  • a critical point K is the boundary between the saturated vapor line 40 and the saturated liquid line 41 .
  • FIG. 3 solid line arrows indicate the direction in which the refrigerant flows
  • dashed line arrows indicate the direction in which air flows
  • examples of temperatures of the refrigerant and air under typical conditions are appended to the arrows.
  • the horizontal axis indicates the enthalpy of the refrigerant
  • the pressure in the state R2 and the pressure in the state R2-1 are actually the same, but for the convenience of illustration, they are not overlapped and shown separately.
  • the operation of the air conditioner 200 will be described by taking as an example a case where the heat exchange fluid is air and the heat exchange fluid is refrigerant.
  • the first heat exchanger 11 acts as a condenser
  • the second heat exchanger 12 and the third heat exchanger 13 act as evaporators.
  • high-temperature and high-pressure gaseous refrigerant is discharged from the compressor 16 (state R1 in FIG. 3).
  • the temperature of the coolant at this time is, for example, 70°C.
  • the high-temperature and high-pressure gas refrigerant (single-phase) discharged from the compressor 16 flows into the first heat exchanger 11 functioning as a condenser.
  • the first heat exchanger 11 heat is exchanged between the high-temperature, high-pressure gas refrigerant that has flowed in and the return air RA that is returned from the room 300 to the outside 301 by the return air fan 15 .
  • the temperature TR of the return air RA is, for example, 27°C.
  • the high-temperature and high-pressure gas refrigerant is condensed into a high-pressure liquid refrigerant (single-phase) (state R2 in FIG. 3).
  • the opening degree OP of the expansion device 17 is set smaller than that in the dehumidifying operation.
  • the pressure P of the refrigerant in the state R2 is increased to the value P1 to promote heat exchange, so that the temperature of the liquid refrigerant flowing out of the first heat exchanger 11 is made approximately the same as the temperature TR of the return air RA. can be lowered to
  • the temperature of the refrigerant flowing out of the first heat exchanger 11 is, for example, 27°C.
  • the opening degree OP of the expansion device 17 is set by the control of the control unit 90 so as to be smaller than that in the dehumidifying operation mode, which will be described later.
  • the value P1 is a value equal to or greater than the value P2 during the dehumidifying operation shown in FIG.
  • the high-pressure liquid refrigerant sent out from the first heat exchanger 11 exchanges heat with the outside air OA and evaporates in the second heat exchanger 12 functioning as an evaporator (state R3 in FIG. 3).
  • the temperature TR of the return air RA is lower than the temperature To of the outside air OA.
  • the temperature T R of the return air RA is 27°C and the temperature T O of the outside air OA is 35°C.
  • the temperature of the liquid refrigerant flowing from the first heat exchanger 11 to the second heat exchanger 12 is approximately the same as the temperature TR of the return air RA and lower than the outside air OA, as described above.
  • the outside air OA is cooled in the heat exchange of the second heat exchanger 12 . Therefore, the temperature T O 1 of the outside air OA that has passed through the second heat exchanger 12 is, for example, 27°C.
  • the liquid refrigerant evaporated and heated in the second heat exchanger 12 becomes a two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant by the throttle device 17 (state R4 in FIG. 3).
  • the two-phase refrigerant flows into the third heat exchanger 13 functioning as an evaporator.
  • heat is exchanged between the flowing two-phase refrigerant and the outside air OA supplied from the outdoor 301 to the indoor 300 by the air supply fan 14 .
  • the liquid refrigerant of the two-phase refrigerant evaporates to become a low-pressure gas refrigerant (single-phase) (state R5 in FIG. 3).
  • the outside air OA is cooled in the third heat exchanger 13 .
  • the temperature T O 2 of the outside air OA that has passed through the third heat exchanger 13 is, for example, 15°C.
  • the air that has passed through the second heat exchanger 12 and the air that has passed through the third heat exchanger 13 are mixed to form supply air SA, which is supplied to the room 300. supplied.
  • the low-pressure gas refrigerant sent out from the third heat exchanger 13 flows into the compressor 16, is compressed into high-temperature and high-pressure gas refrigerant, and is discharged from the compressor 16 again (state R1 in FIG. 3). This cycle is then repeated.
  • control unit 90 controls the opening degree OP of the expansion device 17 based on the discharge refrigerant pressure of the compressor 16 and the outlet refrigerant temperature of the first heat exchanger 11 so that the temperature in the room 300 reaches the set temperature. do.
  • FIG. 4 is a flow chart showing the operation of the control unit 90 in the cooling operation mode of the air conditioner 200 according to Embodiment 1.
  • step S ⁇ b>1 the control unit 90 acquires the refrigerant pressure on the discharge port side of the compressor 16 from the discharge pressure detection unit 86 .
  • step S2 based on the acquired refrigerant pressure, the control unit 90 calculates the saturation temperature at that pressure.
  • step S ⁇ b>3 the control unit 90 acquires the outlet refrigerant temperature of the first heat exchanger 11 from the first refrigerant temperature detection unit 83 .
  • step S4 the control unit 90 calculates the degree of supercooling SC1 at the outlet of the first heat exchanger 11 based on the saturation temperature calculated in step S2 and the outlet refrigerant temperature obtained in step S3.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the calculated outlet supercooling degree SC1 as an index.
  • step S5 the controller 90 compares the outlet supercooling degree SC1 with the threshold value Th1.
  • step S6 the control unit 90 increases the opening degree OP of the diaphragm device 17 from the current value.
  • step S7 the controller 90 reduces the opening degree OP of the diaphragm device 17 from the current value.
  • the amount of increase or decrease in the opening degree OP of the expansion device 17 may be set to a preset constant value, but the control unit 90 determines the amount of increase or decrease according to the difference between the outlet supercooling degree SC1 and the threshold value Th1. You may do so.
  • the threshold Th1 may be a fixed value set in advance based on the design value of the degree of subcooling at the outlet of the first heat exchanger 11 assuming normal cooling operation (that is, the theoretical value during normal operation). can be a variable value.
  • the threshold Th1 is determined by the controller 90 based on the set value for the room temperature of the room 300 set by the user for the air conditioner 200 .
  • a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th1.
  • the data table stores a threshold value Th1 for each set value for room temperature.
  • the arithmetic expression is a function for obtaining the threshold value Th1 using the set value for the room temperature as a parameter.
  • the opening degree OP of the expansion device 17 in the cooling operation mode is set to a smaller value than in the dehumidification operation mode.
  • a boundary value between the opening degree OP of the expansion device 17 in the cooling operation mode and the opening degree OP of the expansion device 17 in the dehumidifying operation mode is defined as a boundary point OP A (see FIG. 8).
  • the opening degree OP of the expansion device 17 in the cooling operation mode is a value within the first range below the boundary point OP A
  • the opening degree OP of the expansion device 17 in the dehumidifying operation mode is greater than the boundary point OP A.
  • a value within the second range is a value within the second range.
  • the control unit 90 may perform the following control.
  • the number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 are determined in advance according to the required ventilation amount of the room 300 .
  • the rotation speeds of the supply air fan 14 and the return air fan 15 can be changed, for example, because a ventilator is provided in addition to the air conditioner 200 .
  • the control unit 90 increases the outlet supercooling degree SC1 by increasing the rotation speeds of the supply air fan 14 and the return air fan 15, and increases the rotation speeds of the supply air fan 14 and the return air fan 15. By decreasing, the outlet supercooling degree SC1 may be decreased.
  • control unit 90 may control the opening degree OP of the expansion device 17 based on the suction pressure of the compressor 16 and the outlet refrigerant temperature of the third heat exchanger 13 .
  • the controller 90 acquires the pressure of the refrigerant sucked by the compressor 16 from the suction pressure detector 87 and calculates the saturation temperature at that pressure.
  • the control unit 90 also acquires the outlet refrigerant temperature of the third heat exchanger 13 from the third refrigerant temperature detection unit 85 .
  • the control unit 90 calculates the outlet superheat degree SHe of the third heat exchanger 13 based on the calculated saturation temperature and the acquired outlet refrigerant temperature.
  • the control unit 90 When the outlet superheat degree SHe is equal to or less than a preset threshold value Th2, the control unit 90 performs control to decrease the opening degree OP of the expansion device 17 in order to prevent the liquid from being sucked into the compressor 16 . On the other hand, when the outlet superheat degree SHe is greater than the threshold value Th2, the control unit 90 maintains the opening degree OP of the expansion device 17 at the current value.
  • control unit 90 may control the opening degree OP of the expansion device 17 based on the discharge pressure of the compressor 16 and the temperature of the refrigerant discharged from the compressor 16 .
  • the control unit 90 acquires the pressure of the refrigerant discharged from the compressor 16 from the discharge pressure detection unit 86 and calculates the saturation temperature at that pressure.
  • the control unit 90 also acquires the temperature of the refrigerant discharged from the compressor 16 from the discharge temperature detection unit 88 .
  • the control unit 90 calculates the degree of discharge superheat SHd of the compressor 16 based on the calculated saturation temperature and the acquired temperature of the refrigerant.
  • the control unit 90 controls the opening degree OP of the throttle device 17 according to the preset threshold value Th3-1 of the ejection temperature and the threshold value Th3-2 of the ejection superheat degree SHd.
  • the ejection temperature detection unit 88 is equal to or higher than the threshold value Th3-1, control is performed to increase the opening degree OP of the expansion device 17 .
  • the refrigerant at the outlet of the third heat exchanger 13 functioning as an evaporator is brought into a wet state, causing the compressor 16 to suck in a small amount of liquid refrigerant, thereby lowering the discharge temperature of the compressor 16 .
  • the opening degree OP of the expansion device 17 is maintained at the current value.
  • the degree of discharge superheat SHd is equal to or less than the threshold value Th3-2, control is performed to decrease the degree of opening OP of the throttle device 17 . As a result, excessive inflow of liquid into the compressor 16 can be prevented.
  • the discharge superheat SHd is greater than the threshold value Th3-2, the opening OP of the expansion device 17 is maintained at the current value.
  • FIG. 5 is an explanatory diagram illustrating the refrigerant flow and the air flow in the dehumidifying operation mode of the air conditioner 200 according to Embodiment 1.
  • FIG. 6 is a Mollier diagram showing refrigerant states in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • FIG. 1 is an explanatory diagram illustrating the refrigerant flow and the air flow in the dehumidifying operation mode of the air conditioner 200 according to Embodiment 1.
  • FIG. 6 is a Mollier diagram showing refrigerant states in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1.
  • solid line arrows indicate the direction of refrigerant flow
  • broken line arrows indicate the direction of air flow
  • the temperatures of the refrigerant and air under typical conditions are appended to the arrows.
  • the horizontal axis indicates the enthalpy of the refrigerant
  • the vertical axis indicates the pressure of the refrigerant.
  • FIG. 6 shows air temperature, refrigerant pressure, enthalpy, and refrigerant temperature.
  • the saturated vapor line 40 and the saturated liquid line 41 are indicated by dashed curved lines.
  • a critical point K is the boundary between the saturated vapor line 40 and the saturated liquid line 41 .
  • the operation of the air conditioner 200 will be described by taking as an example a case where the heat exchange fluid is air and the heat exchange fluid is refrigerant.
  • the first heat exchanger 11 and the second heat exchanger 12 act as condensers, and the third heat exchanger 13 acts as an evaporator.
  • the control unit 90 increases the opening degree OP of the expansion device 17 compared to that in the cooling operation mode, thereby setting the pressure P in the state R2 to a value lower than the value P1 in the cooling operation mode. Make it P2.
  • the temperature of the liquid refrigerant is lowered to a temperature higher than the temperature TO of the outside air OA.
  • the temperature of the liquid refrigerant sent out from the first heat exchanger 11 is, for example, 45°C, and the temperature of the outside air OA is, for example, 35°C.
  • the high-pressure liquid refrigerant sent out from the first heat exchanger 11 flows into the second heat exchanger 12 functioning as a condenser.
  • the liquid refrigerant exchanges heat with the outside air OA and condenses (state R3 in FIG. 6).
  • the temperature (eg, 45° C.) of the liquid refrigerant flowing from the first heat exchanger 11 to the second heat exchanger 12 is higher than the temperature (eg, 35° C.) of the outside air OA, as described above. Therefore, the outside air OA is heated in the second heat exchanger 12 .
  • the temperature T O 1 of the outside air OA that has passed through the second heat exchanger 12 is, for example, 45°C.
  • the condensed liquid refrigerant is depressurized by the expansion device 17 and becomes two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant (state R4 in FIG. 6).
  • the two-phase refrigerant flows into the third heat exchanger 13 functioning as an evaporator.
  • heat is exchanged between the flowing two-phase refrigerant and the outside air OA supplied from the outdoor 301 by the air supply fan 14.
  • the refrigerant evaporates and becomes a low-pressure gas refrigerant (single-phase) (state R5 in FIG. 6).
  • the temperature T O 2 of the outside air OA that has passed through the third heat exchanger 13 is, for example, 15°C.
  • the low-pressure gas refrigerant sent out from the third heat exchanger 13 flows into the compressor 16, is compressed into high-temperature and high-pressure gas refrigerant, and is discharged from the compressor 16 again (state R1 in FIG. 6). This cycle is then repeated.
  • the air heated by the second heat exchanger 12 and the air cooled and dehumidified by the third heat exchanger 13 are mixed and supplied to the room 300 as supply air SA.
  • dehumidifying operation that reduces the humidity in the room 300 while suppressing a temperature drop in the room 300 is possible.
  • control unit 90 controls the opening degree OP of the expansion device 17 based on the discharge refrigerant pressure of the compressor 16 and the outlet refrigerant temperature of the second heat exchanger 12 so that the temperature in the room 300 reaches the set temperature. do.
  • the heating capacity of the second heat exchanger 12 is increased or decreased, so that the temperature of the air heated by the second heat exchanger 12 and supplied to the room 300 is can be adjusted. Thereby, the temperature in the room 300 can be maintained at the set temperature.
  • FIG. 7 is a flowchart showing the operation of the control unit 90 in the dehumidifying operation mode in the air conditioner 200 according to Embodiment 1.
  • the control unit 90 acquires the refrigerant pressure on the discharge port side of the compressor 16 from the discharge pressure detection unit 86 .
  • the control unit 90 calculates the saturation temperature at the obtained pressure based on the obtained refrigerant pressure.
  • the control unit 90 acquires the outlet refrigerant temperature of the second heat exchanger 12 from the second refrigerant temperature detection unit 84 .
  • step S14 the control unit 90 calculates the outlet subcooling degree SC2 of the second heat exchanger 12 based on the saturation temperature calculated in step S12 and the refrigerant temperature obtained in step S13.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the calculated outlet supercooling degree SC2 as an index.
  • step S15 the controller 90 compares the outlet supercooling degree SC2 with the threshold value Th4. When the outlet supercooling degree SC2 is greater than the threshold Th4, the process proceeds to step S16, and when the outlet supercooling degree SC2 is equal to or less than the threshold Th4, the process proceeds to step S17.
  • step S16 the control unit 90 determines that the room temperature in the room 300 has decreased, and increases the opening degree OP of the expansion device 17 from the current value. As a result, the heating capacity of the second heat exchanger 12 increases, and the temperature of the outside air OA that has passed through the second heat exchanger 12 rises.
  • step S17 the controller 90 determines that the room temperature in the room 300 is high, and reduces the opening degree OP of the expansion device 17 from the current value. As a result, the heating capacity of the second heat exchanger 12 is reduced, and the temperature of the outside air OA that has passed through the second heat exchanger 12 is lowered.
  • the amount of increase or decrease in the opening degree OP of the expansion device 17 may be set to a preset constant value, but the control unit 90 determines the amount of increase or decrease according to the difference between the outlet supercooling degree SC2 and the threshold value Th4. You may do so.
  • the threshold Th4 may be a fixed value set in advance based on the design value of the degree of subcooling at the outlet of the second heat exchanger 12 assuming normal dehumidifying operation (that is, the theoretical value during normal operation). can be a variable value.
  • the threshold Th4 is determined by the control unit 90 based on the set value for the room temperature of the room 300 set by the user for the air conditioner 200 .
  • a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th4.
  • the data table stores a threshold value Th4 for each set value for room temperature.
  • the arithmetic expression is a function for obtaining the threshold value Th4 using the set value for the room temperature as a parameter.
  • control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC2 of the second heat exchanger 12 as an index.
  • the dehumidifying operation mode it is possible to perform a dehumidifying operation that reduces the humidity in the room 300 while suppressing a temperature drop in the room 300 .
  • the control unit 90 may perform the following control.
  • the number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 are determined in advance according to the required ventilation amount of the room 300 .
  • the number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 can be changed, for example, because a ventilator is provided in addition to the air conditioner 200 .
  • the outlet supercooling degree SC2 may be controlled by changing the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 instead of the opening degree OP of the expansion device 17.
  • the control unit 90 increases the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 to reduce the outlet supercooling degree SC2. increase.
  • the controller 90 decreases the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 to decrease the outlet supercooling degree SC2.
  • the control of the opening degree OP of the expansion device 17 and the control of the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 may be used in combination without being limited to this case.
  • control unit 90 may control the opening degree OP of the expansion device 17 based on the refrigerant suction pressure of the compressor 16 and the outlet refrigerant temperature of the third heat exchanger 13 . In that case, the control unit 90 calculates the saturation temperature at the pressure based on the refrigerant suction pressure detected by the suction pressure detection unit 87 . Next, the control unit 90 calculates the outlet superheat degree SHe of the third heat exchanger 13 based on the calculated saturation temperature and the refrigerant temperature of the third refrigerant temperature detection unit 85 .
  • the control unit 90 reduces the opening degree OP of the expansion device 17 from the current opening degree in order to prevent the liquid from being sucked into the compressor 16 when the outlet superheat degree SHe is equal to or less than the threshold value Th5. Further, when the outlet superheat degree SHe is greater than the threshold value Th5, the control unit 90 maintains the opening degree OP of the expansion device 17 at the current value.
  • control unit 90 may control the opening degree OP of the expansion device 17 based on the pressure of the refrigerant discharged from the compressor 16 and the temperature of the refrigerant discharged from the compressor 16 .
  • the controller 90 calculates the saturation temperature at the pressure based on the refrigerant pressure detected by the discharge pressure detector 86 .
  • the controller 90 calculates the discharge superheat SHd of the compressor 16 based on the calculated saturation temperature and the refrigerant temperature of the discharge temperature detector 88 .
  • the control unit 90 controls the opening degree OP of the throttle device 17 in accordance with the preset threshold value Th6-1 for the ejection temperature and the threshold value Th6-2 for the ejection superheat degree SHd.
  • the ejection temperature detection unit 88 When the ejection temperature detection unit 88 is equal to or higher than the threshold value Th6-1, control is performed to increase the opening degree OP of the expansion device 17 . As a result, the refrigerant at the outlet of the third heat exchanger 13 functioning as an evaporator is brought into a wet state, causing the compressor 16 to suck in a small amount of liquid refrigerant, thereby lowering the discharge temperature of the compressor 16 .
  • the discharge temperature detection unit 88 When the discharge temperature detection unit 88 is less than the threshold value Th6-1, the opening degree OP of the expansion device 17 is maintained at the current value.
  • the discharge superheat SHd is equal to or less than the threshold value Th6-2, control is performed to decrease the opening degree OP of the expansion device 17 . As a result, excessive inflow of liquid into the compressor 16 can be prevented.
  • the degree of discharge superheat SHd is greater than the threshold value Th6-2, the opening degree OP of the expansion device 17 is maintained at the current
  • FIG. 8 is an explanatory diagram showing the operation mode switching operation according to the opening degree OP of the expansion device 17 in the air conditioner 200 according to Embodiment 1.
  • T o is the temperature of the outside air OA
  • T R is the temperature of the return air RA.
  • a boundary point OP A of the degree of opening OP of the expansion device 17 is a boundary at which the cooling operation mode and the dehumidifying operation mode are switched.
  • the opening degree OP of the expansion device 17 is within a second range larger than the boundary point OP A
  • the dehumidifying operation mode is entered
  • the opening degree OP of the expansion device 17 is within a first range below the boundary point OP A
  • the cooling operation is performed. become a mode.
  • the vertical axis indicates the cooling capacity and heating capacity of the second heat exchanger 12 .
  • the area greater than 0 indicates heating capacity
  • the area below 0 indicates cooling capacity.
  • the opening degree OP of the expansion device 17 when the opening degree OP of the expansion device 17 is within the first range, the pressure in state R2 in FIGS. , heat exchange is facilitated. Therefore, the temperature of the refrigerant after heat exchange becomes approximately the same as the temperature TR of the return air RA. At this time, since the temperature T R of the return air RA is lower than the temperature T O of the outside air OA, the second heat exchanger 12 acts as an evaporator. That is, the operation mode of the air conditioner 200 becomes the cooling operation mode. At this time, if the opening degree OP of the expansion device 17 is increased toward the boundary point OPA , the pressure in the state R2 decreases and the heat exchange amount decreases as the opening degree OP increases.
  • the refrigerant temperature in the state R2 becomes equal to the temperature T O of the outside air OA.
  • the second heat exchanger 12 does not exchange heat.
  • the opening degree OP of the expansion device 17 is increased to a value within the second range, the refrigerant temperature in the state R2 exceeds the temperature TO of the outside air OA, so the second heat exchanger 12 functions as a condenser. works. That is, the operation mode of the air conditioner 200 becomes the dehumidification operation mode.
  • FIG. 9 is a flowchart showing the operation mode switching operation of the control unit 90 in the air conditioner 200 according to Embodiment 1.
  • the control unit 90 acquires the temperature T room and the absolute humidity X room of the room 300, which is the space to be air-conditioned, from the second temperature/humidity detection unit 81 that detects the temperature and humidity of the return air RA.
  • the controller 90 compares the temperature T room of the air-conditioned space with a threshold value Th7.
  • step S23 the control unit 90 compares the absolute humidity X room of the room 300, which is the space to be air-conditioned, with the threshold value Th8.
  • step S25 the control unit 90 proceeds to the process of step S25 and performs operation in the dehumidifying operation mode.
  • step S26 the control unit 90 stops the compressor 16 in the air conditioner 200 so as not to operate the heat pump circuit, and operates at least one of the return air fan 15 and the supply air fan 14 to perform only ventilation. do.
  • the threshold Th7 may be a preset fixed value, or may be determined based on a set value for the room temperature of the room 300 set by the user for the air conditioner 200 .
  • the threshold Th8 may be a preset fixed value, or may be determined based on a set value for the humidity of the room 300 or a set value for the room temperature set by the user for the air conditioner 200. good.
  • the threshold Th7 and the threshold Th8 may be determined using a data table or an arithmetic expression in the same manner as the thresholds Th1 and Th4.
  • FIG. 10 is a side view showing the configuration of the heat transfer tubes of the first heat exchanger 11 and the second heat exchanger 12 in the air conditioner 200 according to Embodiment 1.
  • FIG. 10(a) shows an example of the configuration of the heat transfer tubes 100 of the first heat exchanger 11
  • FIG. 10(b) shows an example of the configuration of the heat transfer tubes 101 of the second heat exchanger 12.
  • FIG. 10(a) shows an example of the configuration of the heat transfer tubes 100 of the first heat exchanger 11
  • FIG. 10(b) shows an example of the configuration of the heat transfer tubes 101 of the second heat exchanger 12.
  • the heat transfer tubes 100 of the first heat exchanger 11 are arranged vertically at regular intervals.
  • the heat transfer tube 100 has a circular tubular shape.
  • the heat transfer tubes 100 are arranged to pass through the fins 102 .
  • the heat transfer tubes 101 of the second heat exchanger 12 are arranged vertically at regular intervals.
  • the heat transfer tubes 101 are arranged to pass through the fins 103 .
  • the heat transfer tube 101 has a flat tube shape having a major axis and a minor axis.
  • the short diameter of heat transfer tube 101 extends in the vertical direction
  • the long diameter of heat transfer tube 101 extends in a direction perpendicular to the vertical direction (that is, in the horizontal direction).
  • heat transfer tube 101 has a longer outer circumference than heat transfer tube 100 .
  • the heat transfer area of the heat transfer tube 101 is correspondingly larger than that of the heat transfer tube 100 .
  • FIG. 10(b) illustrates a case where the heat transfer tube 101 is made of a flat perforated tube.
  • the inside of the heat transfer tube 101 is partitioned by the inner column 101a to form a plurality of small-diameter refrigerant flow paths 101b.
  • the circular heat transfer tube 100 shown in FIG. 10(a) one refrigerant channel 100b having a large diameter is provided.
  • the contact length between the refrigerant and the inside of the tube in one cross section can be doubled or more due to the subdivision as compared with a flat tube that is not subdivided. Thereby, the heat transfer area inside the heat transfer tube 101 can be increased.
  • the maximum value of the heating capacity of the second heat exchanger 12 in the dehumidifying operation mode is greatly affected by the ratio of the heat transfer area to the first heat exchanger 11.
  • the second heat exchanger In order to realize an operating state (dehumidification only) in which the heating capacity of the second heat exchanger 12 and the cooling capacity of the third heat exchanger 13 are balanced, the second heat exchanger must be It is desirable that the heat transfer area of 12 is large.
  • the heat transfer tubes 101 of the second heat exchanger 12 are made flat.
  • the heat transfer area of the heat transfer tube 101 is made larger than that of the heat transfer tube 100 of the first heat exchanger 11. also increase.
  • the heat transfer area can be further increased.
  • the projected area of the heat transfer tubes when viewed from the direction of air flow is smaller for the flat tubes than for the circular tubes. Therefore, when designed with the same airflow resistance as that of a circular tube, the heat transfer tubes 101 can be arranged at a high density with respect to the circular tube. That is, in FIG.
  • heat transfer tubes 101 can be arranged in the area where three heat transfer tubes 100 are provided, in FIG. 10(b). This increases the contact length between the heat transfer tubes 101 and the fins 103 and improves the efficiency of the fins 103 .
  • the heat transfer tubes 100 are inserted into the fins 102 and then expanded so that the heat transfer tubes 100 are brought into close contact with the fins 102 .
  • the fins 103 and the heat transfer tube 101 are welded together by brazing, so that the thermal resistance is reduced.
  • the heat transfer area of the second heat exchanger 12 is larger than that of the first heat exchanger 11, and the heating capacity of the second heat exchanger 12 and the cooling capacity of the third heat exchanger 13 are balanced. It is possible to achieve a stable operating state (only dehumidification).
  • the heat transfer tubes of the third heat exchanger 13 are not particularly limited, and even if they have the same flat tube shape as the heat transfer tubes 101 of the second heat exchanger 12, It may have a circular tubular shape.
  • the second heat exchanger 12 is filled with liquid refrigerant
  • the second heat exchanger 12 in the dehumidifying operation mode, the second heat exchanger 12 is filled with liquid refrigerant or two-phase refrigerant. Therefore, the refrigerant charging amount required for operation differs greatly between the cooling operation mode and the dehumidifying operation mode. If the amount of refrigerant charged is appropriate for one of the operation modes, it becomes difficult to achieve stable operation in the other operation mode. Reducing the volume of the refrigerant flow path 101b of the second heat exchanger 12 is effective in suppressing fluctuations in the required amount of refrigerant due to such operation modes. Specifically, as shown in FIG.
  • the heat transfer tube 101 preferably has a structure having a large number of small-diameter refrigerant flow paths 101b, such as a flat perforated tube. Due to such a structure, the flat perforated pipe can achieve both a large heat transfer area and a small coolant channel volume.
  • the second heat exchanger 12 has a smaller refrigerant passage volume than the first heat exchanger 11, thereby suppressing fluctuations in the amount of refrigerant in the heat exchanger due to differences in operation modes, The stability of the operation of the harmony device 200 can be improved. Moreover, it becomes possible for the first heat exchanger 11 to absorb excess or deficiency of the refrigerant generated in the second heat exchanger 12 .
  • FIG. 10(b) shows an example in which the heat transfer tubes 101 of the second heat exchanger 12 have a flat tube shape.
  • the heat transfer area where the second heat exchanger 12 performs heat exchange is larger than the heat transfer area where the first heat exchanger 11 performs heat exchange
  • FIG.10(b) the case where the heat exchanger tube 101 of the 2nd heat exchanger 12 is comprised from a flat perforated tube is mentioned as an example, and is shown.
  • the heat transfer tube 101 of the second heat exchanger 12 has a flat tube shape, the heat transfer area where the second heat exchanger 12 performs heat exchange is Larger than the heat transfer area for heat exchange. Therefore, it is not always necessary to subdivide the inside of the heat transfer tubes 101 of the second heat exchanger 12 into perforated tubes.
  • FIG. 10(b) shows an example in which the heat transfer tubes 101 of the second heat exchanger 12 are made of flat perforated tubes in order to reduce the volume of the refrigerant flow path.
  • the configuration is not limited to this case, and the volume of each refrigerant flow path 101b of the heat transfer tube 101 of the second heat exchanger 12 is smaller than the volume of each refrigerant flow path of the heat transfer tube 100 of the first heat exchanger 11. If so, other configurations may be used.
  • the second heat exchanger 12 has a larger heat transfer area than the first heat exchanger 11 and a smaller refrigerant flow volume than the first heat exchanger 11. I explained the case where However, this is not the case when designing with a focus on the cooling operation mode.
  • Both the second heat exchanger 12 and the third heat exchanger 13 are arranged in the air supply path 19 .
  • the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air supply path 19 will be described.
  • FIG. 11 is a plan view illustrating an example of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1.
  • FIG. 11 the state which looked at the 2nd heat exchanger 12 and the 3rd heat exchanger 13 from the top is shown.
  • FIG. 11(a) shows an arrangement example of the second heat exchanger 12 and the third heat exchanger 13 in Embodiment 1
  • FIG. 11(b) shows a comparative example.
  • FIGS. 11(a) and (b) white arrows indicate the direction in which the outside air OA flows in the air supply path 19.
  • FIG. 11( a ) the second heat exchanger 12 and the third heat exchanger 13 are arranged side by side in a direction perpendicular to the vertical direction (that is, in the horizontal direction), and outside air OA flows. They are arranged side by side in a direction perpendicular to the direction. Accordingly, at least part of the outside air OA flowing through the air supply path 19 passes through the second heat exchanger 12 only. This can prevent the second heat exchanger 12 from acting as a condenser in the cooling operation mode.
  • Embodiment 1 it is desirable to avoid at least the serial arrangement shown in the comparative example of FIG. 11(b).
  • the second heat exchanger 12 and the third heat exchanger 13 are arranged side by side along the direction of air flow. That is, one of the second heat exchanger 12 and the third heat exchanger 13 is arranged on the upstream side and the other is arranged on the downstream side in the direction of air flow.
  • FIG. 11B if the third heat exchanger 13 is on the upstream side, the air cooled by the third heat exchanger 13 flows to the second heat exchanger 12 .
  • the second heat exchanger 12 functions as a condenser, and operation in the cooling operation mode cannot be performed.
  • the third heat exchanger 13 cools the outside air OA, thereby dehumidifying. Insufficient quantity.
  • FIG. 12 is a side view explaining a modification of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1.
  • FIG. FIG. 12 shows a state in which the second heat exchanger 12 and the third heat exchanger 13 are viewed from the side. You may make it arrange
  • the air conditioner 200 includes one expansion device 17 and three heat exchangers 11 to 13 on the refrigerant circuit, and the first heat exchanger 11 is in the return air path 20.
  • the second heat exchanger 12 and the third heat exchanger 13 are arranged in the air supply path 19 .
  • the air heated by the second heat exchanger 12 and the air cooled by the third heat exchanger 13 are mixed in the duct etc. forming the air supply path 19 before reaching the room 300. and a uniform temperature. Therefore, as shown in FIG. 12, when the second heat exchanger 12 is arranged below the third heat exchanger 13 in the vertical direction, high-temperature air rises due to buoyancy. The air that has passed through the second heat exchanger 12 rises. As a result, mixing of the air heated by the second heat exchanger 12 and the air cooled by the third heat exchanger 13 can be promoted. As a result, it is possible to provide air having a uniform temperature with little unevenness in the room 300 and improve comfort.
  • the refrigerant flows in the same direction in the refrigerant circuit in the cooling operation mode and the dehumidifying operation mode.
  • the opening degree OP of the expansion device 17 is set within the first range, the first heat exchanger 11 acts as a condenser, and the second heat exchanger 12 and the third heat exchanger 13 are Acts as an evaporator.
  • the opening degree OP of the expansion device 17 is set within a second range larger than the first range, the first heat exchanger 11 and the second heat exchanger 12 act as condensers, 3 Heat exchanger 13 acts as an evaporator.
  • the air conditioner 200 according to Embodiment 1 can continuously switch between the dehumidifying operation mode and the cooling operation mode with a simple configuration that does not require switching of the flow path. Therefore, unlike Patent Document 1 described above, it is possible to suppress fluctuations in the pressure of the refrigerant in the heat exchanger that accompany switching of the flow path. As a result, in Embodiment 1, since the temperature fluctuation of the supply air SA supplied to the room 300 by the air conditioner 200 can be suppressed, the supply air SA having a stable temperature is supplied to the room 300, and the temperature inside the room 300 is reduced. of user comfort can be improved.
  • the control unit 90 controls the pressure of the refrigerant on the discharge side or the suction side of the compressor 16, the refrigerant temperature on the outlet side of the second heat exchanger 12, the temperature of the refrigerant on the outlet side of the second heat exchanger 12, the The opening degree OP of the throttle device 17 is controlled based on at least one of the refrigerant temperature on the outlet side of the compressor 13 and the refrigerant temperature on the discharge side of the compressor 16 . Specifically, the control unit 90 reduces the opening degree OP of the expansion device 17 from the current value within the second range so that the second heat exchanger for the outdoor air supplied by the air supply fan 14 Decrease the heating capacity of 12.
  • control unit 90 increases the degree of opening of the expansion device 17 within the second range from the current value so that the outdoor air supplied by the supply fan 14 is heated by the second heat exchanger 12 . increase capacity.
  • the temperature of the air supplied from the second heat exchanger 12 to the room 300 can be controlled, so that the dehumidification operation that reduces the humidity in the room 300 can be performed while suppressing the temperature drop in the room 300 .
  • FIG. 13 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200B according to Embodiment 2. As shown in FIG. Compared with the configuration of FIG. 1 described in Embodiment 1, the configuration of FIG. Since other configurations are the same as those in FIG. 1, they are denoted by the same reference numerals, and descriptions thereof are omitted here.
  • the first on-off valve 21 is provided in the refrigerant pipe 18 between the first heat exchanger 11 and the second heat exchanger 12 .
  • the opening/closing operation of the first opening/closing valve 21 is controlled by the controller 90 .
  • a bypass pipe 23 is a bypass pipe branched from the refrigerant pipe 18 .
  • the bypass pipe 23 branches off from the refrigerant pipe 18 at a point C ⁇ b>1 between the first heat exchanger 11 and the first on-off valve 21 .
  • the bypass pipe 23 is connected to the refrigerant pipe 18 at a point C2 between the second heat exchanger 12 and the expansion device 17 .
  • the second refrigerant temperature detector 84 is arranged downstream of the bypass pipe 23 .
  • the second on-off valve 22 is provided on the bypass pipe 23 .
  • the opening/closing operation of the second opening/closing valve 22 is controlled by the controller 90 .
  • the controller 90 opens the first on-off valve 21 and closes the second on-off valve 22 in the dehumidifying operation mode.
  • the operation in the dehumidifying operation mode of the second embodiment is the same as the operation in the dehumidifying operation mode of the first embodiment.
  • the controller 90 sets the temperature T 0 of the outside air OA to be higher than the temperature T R of the return air RA, and the temperature difference ⁇ T between the temperature T 0 of the outside air OA and the temperature T R of the return air RA. If it is greater than Th9, the first on-off valve 21 is opened and the second on-off valve 22 is closed.
  • the operation in the cooling operation mode of the second embodiment in this case is the same as the operation in the cooling operation mode of the first embodiment.
  • the threshold Th9 is set in advance based on the design value of the temperature difference ⁇ T between the temperature T O of the outside air OA and the temperature T R of the return air RA assuming normal cooling operation (that is, the theoretical value during normal operation). It may be a fixed value, or a variable value.
  • the threshold value Th9 is a set value for the room temperature of the room 300 set by the user for the air conditioner 200 by the control unit 90, or the temperature T O of the outside air OA and the temperature T R of the return air RA. is determined based on the temperature difference between
  • a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th9.
  • the data table stores a threshold value Th9 for each set value or temperature difference with respect to the room temperature.
  • the arithmetic expression is a function for obtaining the threshold value Th9 using the set value or the temperature difference with respect to the room temperature as a parameter.
  • the controller 90 closes the first on-off valve 21 and opens the second on-off valve 22 .
  • the refrigerant flows through the bypass pipe 23 and flows from the bypass pipe 23 through the expansion device 17 into the third heat exchanger 13 . That is, the refrigerant skips the second heat exchanger 12 and flows through the first heat exchanger 11, the bypass pipe 23, the expansion device 17, and the third heat exchanger 13 in this order.
  • the second heat exchanger 12 which originally operates as an evaporator, can be prevented from operating as a condenser in the cooling operation mode.
  • FIG. 14 is a flow chart showing the operation of the control unit 90 in the air conditioner 200B according to Embodiment 2.
  • the controller 90 determines whether the current operation mode of the air conditioner 200B is the dehumidifying operation mode or the cooling operation mode. If the current operation mode of the air conditioner 200B is the dehumidifying operation mode, the control unit 90 proceeds to the process of step S32. On the other hand, when the current operation mode of the air conditioner 200B is the cooling operation mode, the control unit 90 proceeds to the process of step S33.
  • control unit 90 opens the first on-off valve 21 and closes the second on-off valve 22. That is, the operation in the dehumidifying operation mode of the second embodiment is the same as the operation in the dehumidifying operation mode of the first embodiment.
  • step S33 the controller 90 determines that the temperature T O of the outside air OA is higher than the temperature T R of the return air RA, and that the temperature difference ⁇ T between the temperature T O of the outside air OA and the temperature T R of the return air RA is a threshold value Th9. Determine if greater than. If all of these conditions are satisfied, the control section 90 proceeds to the process of step S34. Otherwise, the control section 90 proceeds to the process of step S35.
  • step S34 the control unit 90 opens the first on-off valve 21 and closes the second on-off valve 22.
  • the operation in the cooling operation mode of the second embodiment in this case is the same as the operation in the cooling operation mode of the first embodiment.
  • step S35 the controller 90 determines that it is difficult to operate the second heat exchanger 12 as an evaporator, closes the first on-off valve 21, and opens the second on-off valve 22.
  • the second embodiment basically has the same configuration as the first embodiment, the same effects as those of the first embodiment can be obtained. Furthermore, in Embodiment 2, as shown in FIG. 13, a first on-off valve 21, a second on-off valve 22, and a bypass pipe 23 are added to the configuration of FIG.
  • the control unit 90 closes the first on-off valve 21 and performs control to open the second on-off valve 22 .
  • the second heat exchanger 12 which originally operates as an evaporator, can be prevented from operating as a condenser.
  • FIG. 15 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3.
  • an accumulator 24 is added to the refrigerant pipe 18 between the third heat exchanger 13 and the compressor 16 in FIG.
  • the accumulator 24 stores excess refrigerant in the refrigerant pipe 18 . Since other configurations are the same as those in FIG. 1, they are denoted by the same reference numerals, and descriptions thereof are omitted here.
  • the detection units 80 to 88 are omitted in FIG. 15, they are actually provided.
  • the amount of refrigerant circulating in the refrigerant pipe 18 is reduced by storing the refrigerant in the accumulator 24 .
  • the amount of refrigerant to be charged should be adjusted to the operation mode that requires the largest amount of refrigerant.
  • Refrigerant is stored in and discharged from the accumulator 24 as needed.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC1 or SC2 of the refrigerant at the outlet of the first heat exchanger 11 or the second heat exchanger 12 as an index.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC1 or SC2 of the refrigerant at the outlet of the first heat exchanger 11 or the second heat exchanger 12 as an index.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC1 or SC2 of the refrigerant at the outlet of the first heat exchanger 11 or the second heat exchanger 12 as an index.
  • the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC1 or SC2 of the refrigerant at the outlet of the first heat exchanger 11 or the second heat exchanger 12 as an index.
  • the third embodiment basically has the same configuration as the first embodiment, the same effect as the first embodiment can be obtained. Furthermore, in Embodiment 3, an accumulator 24 is provided between the third heat exchanger 13 and the compressor 16 . As a result, the refrigerant is stored in the accumulator 24 in the dehumidifying operation mode, and the refrigerant stored in the accumulator 24 is released to the refrigerant pipe 18 in the cooling operation mode, thereby preventing a shortage of refrigerant.

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Abstract

This air conditioning device includes: an air supply fan and an air supply path; an air return fan and an air return path; and a heat pump circuit. A first heat exchanger is disposed in the air return path, and a second heat exchanger and a third heat exchanger are disposed in the air supply path. The air conditioning device has, as operation modes, a cooling operation mode for indoor cooling and a dehumidifying operation mode for indoor dehumidifying. In the dehumidifying operation mode and the cooling operation mode, refrigerant flows through refrigerant piping in a direction of refrigerant discharged from a compressor flowing into the first heat exchanger and refrigerant flowing out from the third heat exchanger being taken into the compressor. In the cooling operation mode, the first heat exchanger acts as a condenser and the second heat exchanger and the third heat exchanger act as evaporators. In the dehumidifying operation mode, the first heat exchanger and the second heat exchanger act as condensers, and the third heat exchanger acts as an evaporator.

Description

空気調和装置air conditioner

 本開示は、除湿運転モードと冷房運転モードとを有する空気調和装置に関する。 The present disclosure relates to an air conditioner having a dehumidifying operation mode and a cooling operation mode.

 例えば、室内の換気を行う従来の外気調和機において、ヒートポンプ回路で、熱交換器を用いて室内から室外に還る還気から熱回収を行う構成が知られている。このヒートポンプ回路の冷媒流れにおいては、室外機に搭載された圧縮機から吐出された高温高圧のガス冷媒が、室内機に搭載された熱交換器に流入される。当該熱交換器は凝縮器として機能するため、流入された冷媒は当該熱交換器で凝縮されて液冷媒となる。その後、当該液冷媒は、膨張弁によって減圧され、ガス冷媒と液冷媒とが混在する気液二相状態となる。そして、気液二相状態の冷媒は、室外機に搭載されて蒸発器として機能する熱交換器に流入される。当該熱交換器では、気液二相状態の冷媒のうちの液冷媒が蒸発されて低圧のガス冷媒となる。この後、当該熱交換器から送り出されたガス冷媒は圧縮機に流れ込み、圧縮機で圧縮されて、高温高圧のガス冷媒となり、再び、圧縮機から吐出される。以下、このサイクルが繰り返される。 For example, in a conventional outdoor air conditioner that ventilates a room, a heat pump circuit is known that uses a heat exchanger to recover heat from return air returning from the room to the outside. In the refrigerant flow of the heat pump circuit, high-temperature and high-pressure gas refrigerant discharged from the compressor mounted on the outdoor unit flows into the heat exchanger mounted on the indoor unit. Since the heat exchanger functions as a condenser, the inflow refrigerant is condensed in the heat exchanger to become liquid refrigerant. After that, the liquid refrigerant is depressurized by the expansion valve, and becomes a gas-liquid two-phase state in which gas refrigerant and liquid refrigerant are mixed. Then, the gas-liquid two-phase refrigerant flows into a heat exchanger mounted on the outdoor unit and functioning as an evaporator. In the heat exchanger, the liquid refrigerant of the gas-liquid two-phase refrigerant is evaporated to become a low-pressure gas refrigerant. Thereafter, the gas refrigerant sent out from the heat exchanger flows into the compressor, is compressed by the compressor, becomes high-temperature and high-pressure gas refrigerant, and is discharged from the compressor again. This cycle is then repeated.

 また、空気流れについて説明すると、外気調和機は、送風機により室外から外気を取り込み、熱交換器で冷却あるいは加熱して室内に給気する。また、外気調和機は、室内から還気を取り込み、熱交換器で冷却あるいは加熱して、室外へ排気する。 Also, to explain the air flow, the outside air conditioner takes in outside air from the outside with a fan, cools or heats it with a heat exchanger, and supplies it to the room. Also, the outdoor air conditioner takes in return air from the room, cools or heats it with a heat exchanger, and exhausts it to the outside.

 ところで、このような外気調和機は、別途設置された室内空気循環型の空気調和装置によって適温に保たれた室内に対して、外気を導入することが多い。このとき、外気調和機が、室内空気に近い温度および湿度になるように、外気の温度および湿度を調整することで、ユーザーに快適で衛生的な空気を供給することができる。そのため、室内と室外との温度差および湿度差に応じて、冷却と除湿を行う運転モードと、除湿のみを行って温度を一定に保つ運転モードなど、複数の運転モードを有する外気調和機が知られている。 By the way, such an outside air conditioner often introduces outside air into a room maintained at an appropriate temperature by a separately installed room air circulation type air conditioner. At this time, the outdoor air conditioner adjusts the temperature and humidity of the outdoor air so that the temperature and humidity of the outdoor air are close to those of the indoor air, thereby supplying comfortable and hygienic air to the user. For this reason, outdoor air conditioners with multiple operation modes, such as an operation mode that cools and dehumidifies according to the difference in temperature and humidity between indoors and outdoors, and an operation mode that only dehumidifies and maintains a constant temperature, are known. It is

 例えば、特許文献1に記載の換気空調装置は、そのような外気調和機の機能を有する空気調和装置である。特許文献1に記載の空気調和装置は、温度調整と湿度調整とを両立するべく、四方弁と電磁弁とを操作することで冷媒の循環方向が切り換え可能な冷媒回路と、空気の流通経路を切り換える切り替え装置とを用いて、複数の運転モードを実現している。 For example, the ventilation air conditioner described in Patent Document 1 is an air conditioner that has such an outside air conditioner function. The air conditioner described in Patent Document 1 has a refrigerant circuit in which the circulation direction of the refrigerant can be switched by operating a four-way valve and a solenoid valve in order to achieve both temperature control and humidity control, and an air circulation path. A plurality of operation modes are realized by using a switching device for switching.

特開2009-58175号公報JP 2009-58175 A

 しかしながら、特許文献1の空気調和装置では、冷房運転から除湿運転への切り替え時に、冷媒の循環方向を切り替える。そのため、当該循環方向の切り替えに伴って、熱交換器内の冷媒圧力が大きく変動する。その結果、空気調和装置から室内に供給される給気の温度変動が不連続となり、ユーザーの快適性が低下する。また、冷媒の循環方向の切り替え機能と空気の流通経路の切り替え機能とを有しているため、多くの駆動部を必要とし、駆動部の故障による機能損失の可能性が高まる。 However, in the air conditioner of Patent Document 1, the circulation direction of the refrigerant is switched when switching from the cooling operation to the dehumidifying operation. Therefore, the refrigerant pressure in the heat exchanger greatly fluctuates with the switching of the circulation direction. As a result, the temperature fluctuation of the supplied air supplied from the air conditioner to the room becomes discontinuous, and the user's comfort is reduced. In addition, since it has a function of switching the circulation direction of the refrigerant and a function of switching the air circulation path, it requires a large number of driving units, which increases the possibility of functional loss due to failure of the driving units.

 本開示は、上記課題を解決するためになされたものであり、冷房運転と除湿運転との切り替え時に冷媒流路の切り替えを必要としない簡易な構成で、冷房運転と除湿運転との切り替え時の給気温度の変動を抑え、ユーザーに対して快適な空気の供給が可能な空気調和装置を提供することを目的とする。 The present disclosure has been made to solve the above problems, and has a simple configuration that does not require switching of refrigerant flow paths when switching between cooling operation and dehumidifying operation, and when switching between cooling operation and dehumidifying operation. An object of the present invention is to provide an air conditioner capable of supplying comfortable air to a user by suppressing fluctuations in supply air temperature.

 本開示に係る空気調和装置は、室外の空気を室内に給気する給気ファンおよび給気経路と、前記室内の空気を前記室外に還気する還気ファンおよび還気経路と、圧縮機、第1熱交換器、第2熱交換器、絞り装置、第3熱交換器の順に冷媒配管によってこれらが接続されたヒートポンプ回路と、前記給気ファン、前記還気ファン、および、前記ヒートポンプ回路の動作の制御を行う制御部とを備えた空気調和装置であって、前記第1熱交換器は、前記還気経路内に配置され、前記第1熱交換器の内部を流れる冷媒と前記還気経路内を流れる空気との間で熱交換を行い、前記第2熱交換器および前記第3熱交換器は、前記給気経路内に配置され、それぞれ、前記第2熱交換器および前記第3熱交換器の内部を流れる冷媒と前記給気経路内を流れる空気との間で熱交換を行い、前記空気調和装置は、運転モードとして、前記室内を冷房する冷房運転モードと前記室内を除湿する除湿運転モードとを有し、前記除湿運転モードおよび前記冷房運転モードにおいて、前記圧縮機から吐出された冷媒が前記第1熱交換器に流入されて、前記第3熱交換器から流出した冷媒が前記圧縮機に吸入される方向に、前記冷媒配管を冷媒が流れ、前記冷房運転モードにおいて、前記第1熱交換器は凝縮器として作用し、前記第2熱交換器および前記第3熱交換器が蒸発器として作用し、前記除湿運転モードにおいて、前記第1熱交換器および前記第2熱交換器は凝縮器として作用し、前記第3熱交換器が蒸発器として作用するものである。 An air conditioner according to the present disclosure includes an air supply fan and an air supply path for supplying outdoor air to a room, a return air fan and a return air path for returning the indoor air to the outdoor, a compressor, A heat pump circuit in which a first heat exchanger, a second heat exchanger, a throttle device, and a third heat exchanger are connected in this order by refrigerant piping, the supply air fan, the return air fan, and the heat pump circuit. and a control unit that controls operation, wherein the first heat exchanger is arranged in the return air path, and the refrigerant and the return air flowing inside the first heat exchanger are arranged in the return air path. The second heat exchanger and the third heat exchanger are arranged in the air supply path, and the second heat exchanger and the third heat exchanger are arranged in the air supply path, respectively. Heat is exchanged between the refrigerant flowing inside the heat exchanger and the air flowing inside the air supply path, and the air conditioner has two operation modes, one for cooling the room and one for dehumidifying the room. and a dehumidifying operation mode, wherein in the dehumidifying operation mode and the cooling operation mode, the refrigerant discharged from the compressor flows into the first heat exchanger, and the refrigerant flowing out of the third heat exchanger is Refrigerant flows through the refrigerant pipe in the direction of being sucked into the compressor, and in the cooling operation mode, the first heat exchanger acts as a condenser, and the second heat exchanger and the third heat exchanger acts as an evaporator, and in the dehumidifying operation mode, the first heat exchanger and the second heat exchanger act as condensers, and the third heat exchanger acts as an evaporator.

 本開示に係る空気調和装置によれば、冷房運転と除湿運転との切り替え時に冷媒流路の切り替えを必要としない簡易な構成で、除湿運転モードと冷房運転モードとを連続的に移行することができる。これにより、給気温度の変動を抑制し、ユーザーの快適性を向上させることができる。 According to the air conditioner according to the present disclosure, it is possible to continuously switch between the dehumidifying operation mode and the cooling operation mode with a simple configuration that does not require switching of the refrigerant flow path when switching between the cooling operation and the dehumidifying operation. can. As a result, fluctuations in the supply air temperature can be suppressed, and user comfort can be improved.

実施の形態1に係る空気調和装置200の構成の一例を示す冷媒回路図である。1 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200の冷房運転モードにおける冷媒の流れおよび空気の流れを説明する説明図である。FIG. 4 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1; 実施の形態1に係る空気調和装置200の冷房運転モードにおける冷媒状態を示すモリエル線図である。4 is a Mollier diagram showing refrigerant states in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における冷房運転モード時の制御部90の動作を示すフローチャートである。4 is a flowchart showing the operation of the control unit 90 in the cooling operation mode of the air conditioner 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200の除湿運転モードにおける冷媒の流れおよび空気の流れを説明する説明図である。FIG. 4 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1; 実施の形態1に係る空気調和装置200の除湿運転モードにおける冷媒状態を示すモリエル線図である。4 is a Mollier diagram showing refrigerant states in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における除湿運転モード時の制御部90の動作を示すフローチャートである。4 is a flow chart showing the operation of the control unit 90 in the dehumidifying operation mode in the air conditioner 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における絞り装置17の開度OPによる運転モードの切替動作を示す説明図である。4 is an explanatory diagram showing operation mode switching operation based on the opening degree OP of the expansion device 17 in the air conditioner 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における制御部90の運転モードの切替動作を示すフローチャートである。4 is a flowchart showing operation mode switching operation of the control unit 90 in the air conditioner 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における第1熱交換器11および第2熱交換器12の伝熱管の構成を示す側面図である。2 is a side view showing the configuration of heat transfer tubes of first heat exchanger 11 and second heat exchanger 12 in air-conditioning apparatus 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における第2熱交換器12および第3熱交換器13の配置の一例を説明する平面図である。2 is a plan view illustrating an example of the arrangement of second heat exchanger 12 and third heat exchanger 13 in air-conditioning apparatus 200 according to Embodiment 1. FIG. 実施の形態1に係る空気調和装置200における第2熱交換器12および第3熱交換器13の配置の変形例を説明する側面図である。4 is a side view illustrating a modification of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1. FIG. 実施の形態2に係る空気調和装置200Bの構成の一例を示す冷媒回路図である。FIG. 7 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200B according to Embodiment 2; 実施の形態2に係る空気調和装置200Bにおける制御部90の動作を示すフローチャートである。9 is a flow chart showing the operation of the control unit 90 in the air conditioner 200B according to Embodiment 2. FIG. 実施の形態3に係る空気調和装置200Cの構成の一例を示す冷媒回路図である。FIG. 11 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3; 実施の形態1に係る空気調和装置200の変形例である空気調和装置200Aの構成の一例を示す冷媒回路図である。2 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1. FIG.

 以下、本開示に係る空気調和装置の実施の形態について図面を参照して説明する。本開示は、以下の実施の形態に限定されるものではなく、本開示の主旨を逸脱しない範囲で種々に変形することが可能である。また、本開示は、以下の実施の形態およびその変形例に示す構成のうち、組み合わせ可能な構成のあらゆる組み合わせを含むものである。また、各図において、同一の符号を付したものは、同一の又はこれに相当するものであり、これは明細書の全文において共通している。なお、各図面では、各構成部材の相対的な寸法関係または形状等が実際のものとは異なる場合がある。 An embodiment of an air conditioner according to the present disclosure will be described below with reference to the drawings. The present disclosure is not limited to the following embodiments, and various modifications can be made without departing from the gist of the present disclosure. In addition, the present disclosure includes all combinations of configurations that can be combined among configurations shown in the following embodiments and modifications thereof. Also, in each figure, the same reference numerals denote the same or corresponding parts, which are common throughout the specification. In each drawing, the relative dimensional relationship, shape, etc. of each component may differ from the actual one.

 実施の形態1.
 [空気調和装置200の構成]
 はじめに、実施の形態1に係る空気調和装置200の構成について説明する。図1は、実施の形態1に係る空気調和装置200の構成の一例を示す冷媒回路図である。実施の形態1では、空気調和装置200は、例えば、室内を換気する外気調和機としての機能を有するものである。空気調和装置200は、運転モードとして、冷房運転モードと除湿運転モードとを有している。
Embodiment 1.
[Configuration of air conditioner 200]
First, the configuration of the air conditioner 200 according to Embodiment 1 will be described. FIG. 1 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200 according to Embodiment 1. As shown in FIG. In Embodiment 1, the air conditioner 200 functions as an outdoor air conditioner that ventilates a room, for example. The air conditioner 200 has a cooling operation mode and a dehumidification operation mode as operation modes.

 図1に示すように、空気調和装置200は、例えば、室内300と室外301との間の境界に設置されている。室内300は、空気調和装置200の被空調空間である。空気調和装置200は、室内300に設置されていてもよい。 As shown in FIG. 1, the air conditioner 200 is installed, for example, at the boundary between an indoor space 300 and an outdoor space 301 . A room 300 is a space to be air-conditioned by the air conditioner 200 . The air conditioner 200 may be installed indoors 300 .

 空気調和装置200は、圧縮機16と、絞り装置17と、第1熱交換器11と、第2熱交換器12と、第3熱交換器13とを含む、ヒートポンプ回路を備えている。圧縮機16、第1熱交換器11、第2熱交換器12、絞り装置17、および、第3熱交換器13が冷媒配管18によって接続されて、冷媒回路が形成されている。 The air conditioner 200 includes a heat pump circuit including a compressor 16, an expansion device 17, a first heat exchanger 11, a second heat exchanger 12, and a third heat exchanger 13. Compressor 16, first heat exchanger 11, second heat exchanger 12, expansion device 17, and third heat exchanger 13 are connected by refrigerant pipe 18 to form a refrigerant circuit.

 空気調和装置200においては、冷房運転モードと除湿運転モードとにおいて、冷媒の流れる方向は同じである。具体的には、冷房運転モードおよび除湿運転モードにおいて、冷媒は、圧縮機16、第1熱交換器11、第2熱交換器12、絞り装置17、第3熱交換器13、圧縮機16の順に流れる。 In the air conditioner 200, the refrigerant flows in the same direction in the cooling operation mode and the dehumidifying operation mode. Specifically, in the cooling operation mode and the dehumidifying operation mode, the refrigerant is flow in order.

 図1に示すように、空気調和装置200は、室外301の空気を室内300に給気する給気経路19および給気ファン14を備えている。給気ファン14は、給気経路19内に配置されている。また、空気調和装置200は、室内300の空気を室外301に還気する還気経路20および還気ファン15を備えている。還気ファン15は、還気経路20内に配置されている。以下、図1を用いて、これらの構成要素について説明する。 As shown in FIG. 1 , the air conditioner 200 includes an air supply path 19 and an air supply fan 14 for supplying air from the outdoor 301 to the indoor 300 . The air supply fan 14 is arranged in the air supply path 19 . The air conditioner 200 also includes a return air path 20 and a return air fan 15 for returning the air in the room 300 to the outside 301 . The return air fan 15 is arranged in the return air path 20 . These components will be described below with reference to FIG.

 なお、図1における4つの矢印は、それぞれ、外気OA、給気SA、還気RA、および、排気EAの通風方向を示している。外気OAは、給気ファン14により室外301から第2熱交換器12および第3熱交換器13へ供給される空気であり、給気経路19内を、室外301から室内300に向かう方向に流れる。また、給気SAは、給気ファン14により第2熱交換器12および第3熱交換器13から室内300へ供給される空気であり、給気経路19内を室外301から室内300に向かう方向に流れる。また、還気RAは、還気ファン15により室内300から第1熱交換器11へ供給される空気であり、還気経路20内を室内300から室外301に向かう方向に流れる。排気EAは、還気ファン15により第1熱交換器11から室外301へ排気される空気であり、還気経路20内を室内300から室外301に向かう方向に流れる。 The four arrows in FIG. 1 respectively indicate the ventilation directions of the outside air OA, the supply air SA, the return air RA, and the exhaust air EA. The outside air OA is air supplied from the outdoor 301 to the second heat exchanger 12 and the third heat exchanger 13 by the air supply fan 14, and flows in the air supply path 19 in the direction from the outdoor 301 to the indoor 300. . In addition, the supply air SA is the air supplied from the second heat exchanger 12 and the third heat exchanger 13 to the room 300 by the supply fan 14, and is directed in the air supply path 19 from the outdoor 301 to the indoor 300. flow to The return air RA is air supplied from the room 300 to the first heat exchanger 11 by the return air fan 15 and flows in the return air path 20 in the direction from the room 300 to the outside 301 . The exhaust EA is air that is discharged from the first heat exchanger 11 to the outdoor 301 by the return air fan 15 , and flows in the return air path 20 in the direction from the indoor 300 to the outdoor 301 .

 給気経路19は、室外301と室内300とを連絡する風路である。給気経路19は、例えば、ダクトから構成されている。給気ファン14は、給気経路19内に設けられ、室外301から室内300へ空気を送風する。給気ファン14は、第2熱交換器12と第3熱交換器13とに、外気OAを供給する。 The air supply path 19 is an air path that connects the outdoor 301 and the indoor 300 . The air supply path 19 is composed of, for example, a duct. The air supply fan 14 is provided in the air supply path 19 and blows air from the outdoor 301 to the indoor 300 . The air supply fan 14 supplies the outside air OA to the second heat exchanger 12 and the third heat exchanger 13 .

 還気経路20は、室内300と室外301とを連絡する風路である。還気経路20は、例えば、ダクトから構成されている。還気ファン15は、還気経路20内に設けられ、室内300から室外301へ空気を送風する。還気ファン15は、第1熱交換器11に還気RAを供給する。 The return air path 20 is an air path that connects the indoor 300 and the outdoor 301 . The return air path 20 is composed of, for example, a duct. The return air fan 15 is provided in the return air path 20 and blows air from the indoor 300 to the outdoor 301 . The return air fan 15 supplies the return air RA to the first heat exchanger 11 .

 給気ファン14および還気ファン15の形態としては、遠心送風機、軸流送風機、横流送風機のいずれでもよく、給気ファン14の形態と還気ファン15の形態とは同じであっても、異なっていてもよい。また、給気ファン14は、第2熱交換器12および第3熱交換器13の上流側にあっても下流側にあってもよい。同様に、還気ファン15は、第1熱交換器11の上流側にあっても下流側にあってもよい。 The form of the supply air fan 14 and the return air fan 15 may be any of a centrifugal fan, an axial flow fan, and a cross flow fan. may be Also, the air supply fan 14 may be located upstream or downstream of the second heat exchanger 12 and the third heat exchanger 13 . Similarly, the return air fan 15 may be upstream or downstream of the first heat exchanger 11 .

 圧縮機16は、吸入口と吐出口とを有している。圧縮機16は、冷媒を吸入口から吸入して、当該冷媒を圧縮し、圧縮した冷媒を吐出口から吐出する。圧縮機16は、例えば、ロータリー圧縮機、スクロール圧縮機、スクリュー圧縮機、または、往復圧縮機等で構成することができる。圧縮機16が、インバータ圧縮機の場合、インバータ回路などにより、運転周波数を任意に変化させ、圧縮機16の単位時間あたりの冷媒を送り出す容量を変化させてもよい。その場合、圧縮機16の運転周波数は、後述する制御部90で制御される。 The compressor 16 has a suction port and a discharge port. The compressor 16 sucks the refrigerant through the suction port, compresses the refrigerant, and discharges the compressed refrigerant through the discharge port. The compressor 16 can be configured by, for example, a rotary compressor, a scroll compressor, a screw compressor, or a reciprocating compressor. When the compressor 16 is an inverter compressor, the operating frequency may be arbitrarily changed by an inverter circuit or the like to change the refrigerant delivery capacity of the compressor 16 per unit time. In that case, the operating frequency of the compressor 16 is controlled by the controller 90, which will be described later.

 第1熱交換器11は、冷媒配管18を介して、圧縮機16の吐出口に接続されている。第1熱交換器11には、圧縮機16から吐出された高温高圧の冷媒が流入される。図1に示すように、第1熱交換器11は、還気経路20内に配置されている。第1熱交換器11は、内部に、冷媒が流れる伝熱管を有している。第1熱交換器11は、例えば、フィンアンドチューブ型熱交換器である。第1熱交換器11は、伝熱管を流れる冷媒と還気RAとの間で熱交換を行う。第1熱交換器11は、冷房運転モードおよび除湿運転モードにおいて、凝縮器として機能する。 The first heat exchanger 11 is connected to the discharge port of the compressor 16 via refrigerant piping 18 . High-temperature, high-pressure refrigerant discharged from the compressor 16 flows into the first heat exchanger 11 . As shown in FIG. 1 , the first heat exchanger 11 is arranged within the return air path 20 . The first heat exchanger 11 has therein heat transfer tubes through which a refrigerant flows. The first heat exchanger 11 is, for example, a fin-and-tube heat exchanger. The first heat exchanger 11 exchanges heat between the refrigerant flowing through the heat transfer tubes and the return air RA. The first heat exchanger 11 functions as a condenser in the cooling operation mode and the dehumidifying operation mode.

 第2熱交換器12は、冷房運転モードにおける冷媒の流れる方向において、第1熱交換器11の下流側に配置されている。第2熱交換器12には、第1熱交換器11から流出された冷媒が流入される。また、第2熱交換器12は、給気経路19内に配置されている。第2熱交換器12は、内部に、冷媒が流れる伝熱管を有している。第2熱交換器12は、例えば、フィンアンドチューブ型熱交換器である。第2熱交換器12は、伝熱管を流れる冷媒と外気OAとの間で熱交換を行う。第2熱交換器12は、冷房運転モードにおいては蒸発器として機能し、除湿運転モードにおいては凝縮器として機能する。 The second heat exchanger 12 is arranged downstream of the first heat exchanger 11 in the direction of refrigerant flow in the cooling operation mode. The refrigerant discharged from the first heat exchanger 11 flows into the second heat exchanger 12 . Also, the second heat exchanger 12 is arranged in the air supply path 19 . The second heat exchanger 12 has therein heat transfer tubes through which a refrigerant flows. The second heat exchanger 12 is, for example, a fin-and-tube heat exchanger. The second heat exchanger 12 exchanges heat between the refrigerant flowing through the heat transfer tubes and the outside air OA. The second heat exchanger 12 functions as an evaporator in the cooling operation mode, and functions as a condenser in the dehumidification operation mode.

 第3熱交換器13は、冷房運転モードにおける冷媒の流れる方向において、第2熱交換器12の下流側に配置されている。第3熱交換器13には、第2熱交換器12から流出された冷媒が、絞り装置17を介して流入される。また、第3熱交換器13は、給気経路19内に配置されている。第3熱交換器13は、内部に、冷媒が流れる伝熱管を有している。第3熱交換器13は、例えば、フィンアンドチューブ型熱交換器である。第3熱交換器13は、伝熱管を流れる冷媒と外気OAとの間で熱交換を行う。第3熱交換器13は、冷房運転モードおよび除湿運転モードにおいて、蒸発器として機能する。 The third heat exchanger 13 is arranged downstream of the second heat exchanger 12 in the direction of refrigerant flow in the cooling operation mode. The refrigerant discharged from the second heat exchanger 12 flows into the third heat exchanger 13 via the expansion device 17 . Also, the third heat exchanger 13 is arranged in the air supply path 19 . The third heat exchanger 13 has therein heat transfer tubes through which a refrigerant flows. The third heat exchanger 13 is, for example, a fin-and-tube heat exchanger. The third heat exchanger 13 exchanges heat between the refrigerant flowing through the heat transfer tubes and the outside air OA. The third heat exchanger 13 functions as an evaporator in the cooling operation mode and the dehumidifying operation mode.

 絞り装置17は、第2熱交換器12と第3熱交換器13との間に配置されている。絞り装置17は、第1熱交換器11および第2熱交換器12を経由した冷媒を膨張させて減圧する。絞り装置17は、例えば冷媒の流量を調整可能な電動膨張弁で構成することができる。なお、絞り装置17としては、電動膨張弁だけでなく、受圧部にダイアフラムを採用した機械式膨張弁等の他の膨張弁を適用することも可能である。 The expansion device 17 is arranged between the second heat exchanger 12 and the third heat exchanger 13 . The expansion device 17 expands and decompresses the refrigerant that has passed through the first heat exchanger 11 and the second heat exchanger 12 . The throttle device 17 can be composed of, for example, an electric expansion valve capable of adjusting the flow rate of the refrigerant. As the expansion device 17, it is possible to apply not only the electric expansion valve but also other expansion valves such as a mechanical expansion valve employing a diaphragm as a pressure receiving portion.

 また、図1に示すように、空気調和装置200は、複数の検出部80~88を有している。各検出部80~88の検出結果は、制御部90に入力される。以下、これらの検出部80~88について説明する。 In addition, as shown in FIG. 1, the air conditioner 200 has a plurality of detectors 80-88. The detection results of the detection units 80 to 88 are input to the control unit 90 . These detection units 80 to 88 will be described below.

 第1温度湿度検出部80は、給気経路19内に配置されている。第1温度湿度検出部80は、空気の流れる方向において、第2熱交換器12および第3熱交換器13の下流に配置されている。第1温度湿度検出部80は、給気SAの温度と湿度とを検出する。第1温度湿度検出部80は、例えば、温度センサおよび湿度センサから構成される。 The first temperature/humidity detector 80 is arranged in the air supply path 19 . The first temperature/humidity detector 80 is arranged downstream of the second heat exchanger 12 and the third heat exchanger 13 in the direction of air flow. The first temperature/humidity detector 80 detects the temperature and humidity of the supplied air SA. The first temperature/humidity detector 80 is composed of, for example, a temperature sensor and a humidity sensor.

 第2温度湿度検出部81は、還気経路20内に配置されている。第2温度湿度検出部81は、空気の流れる方向において、第1熱交換器11の上流に配置されている。第2温度湿度検出部81は、還気RAの温度と湿度とを検出する。第2温度湿度検出部81は、例えば、温度センサおよび湿度センサから構成される。 The second temperature/humidity detection unit 81 is arranged in the return air path 20 . The second temperature/humidity detector 81 is arranged upstream of the first heat exchanger 11 in the direction of air flow. The second temperature/humidity detector 81 detects the temperature and humidity of the return air RA. The second temperature/humidity detector 81 is composed of, for example, a temperature sensor and a humidity sensor.

 外気温度検出部82は、給気経路19内に配置されている。外気温度検出部82は、空気の流れる方向において、第2熱交換器12および第3熱交換器13の上流に配置されている。外気温度検出部82は、外気OAの温度を検出する。外気温度検出部82は、例えば、温度センサから構成される。 The outside air temperature detector 82 is arranged inside the air supply path 19 . The outside air temperature detector 82 is arranged upstream of the second heat exchanger 12 and the third heat exchanger 13 in the direction of air flow. The outside air temperature detector 82 detects the temperature of the outside air OA. The outside air temperature detector 82 is composed of, for example, a temperature sensor.

 第1冷媒温度検出部83は、第1熱交換器11と第2熱交換器12との間の冷媒配管18に取り付けられている。第1冷媒温度検出部83は、冷房運転モードにおける冷媒の流れる方向において、第1熱交換器11の下流に配置されている。第1冷媒温度検出部83は、第1熱交換器11の出口冷媒温度を検出する。第1冷媒温度検出部83は、例えば、温度センサから構成される。 The first refrigerant temperature detector 83 is attached to the refrigerant pipe 18 between the first heat exchanger 11 and the second heat exchanger 12 . The first refrigerant temperature detector 83 is arranged downstream of the first heat exchanger 11 in the direction of refrigerant flow in the cooling operation mode. The first refrigerant temperature detector 83 detects the outlet refrigerant temperature of the first heat exchanger 11 . The first coolant temperature detection unit 83 is composed of, for example, a temperature sensor.

 第2冷媒温度検出部84は、第2熱交換器12と第3熱交換器13との間の冷媒配管18に取り付けられている。第2冷媒温度検出部84は、冷房運転モードにおける冷媒の流れる方向において、例えば、第2熱交換器12の下流で、且つ、絞り装置17の上流に配置されている。第2冷媒温度検出部84は、第2熱交換器12の出口冷媒温度を検出する。第2冷媒温度検出部84は、例えば、温度センサから構成される。 The second refrigerant temperature detector 84 is attached to the refrigerant pipe 18 between the second heat exchanger 12 and the third heat exchanger 13 . The second refrigerant temperature detector 84 is arranged, for example, downstream of the second heat exchanger 12 and upstream of the expansion device 17 in the direction of refrigerant flow in the cooling operation mode. The second refrigerant temperature detector 84 detects the outlet refrigerant temperature of the second heat exchanger 12 . The second coolant temperature detection unit 84 is composed of, for example, a temperature sensor.

 第3冷媒温度検出部85は、第3熱交換器13と圧縮機16との間の冷媒配管18に取り付けられている。第3冷媒温度検出部85は、冷房運転モードにおける冷媒の流れる方向において、第3熱交換器13の下流に配置されている。第3冷媒温度検出部85は、第3熱交換器13の出口冷媒温度を検出する。第3冷媒温度検出部85は、例えば、温度センサから構成される。 The third refrigerant temperature detector 85 is attached to the refrigerant pipe 18 between the third heat exchanger 13 and the compressor 16 . The third refrigerant temperature detector 85 is arranged downstream of the third heat exchanger 13 in the direction of refrigerant flow in the cooling operation mode. The third refrigerant temperature detector 85 detects the outlet refrigerant temperature of the third heat exchanger 13 . The third coolant temperature detection unit 85 is composed of, for example, a temperature sensor.

 吐出圧力検出部86は、圧縮機16の吐出口側に配置されている。吐出圧力検出部86は、例えば、圧縮機16と第1熱交換器11との間の冷媒配管18に取り付けられている。吐出圧力検出部86は、圧縮機16から吐出される冷媒の圧力を検出する。吐出圧力検出部86は、例えば、圧力センサから構成される。 The discharge pressure detector 86 is arranged on the discharge port side of the compressor 16 . The discharge pressure detector 86 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the first heat exchanger 11 . A discharge pressure detector 86 detects the pressure of the refrigerant discharged from the compressor 16 . The discharge pressure detection unit 86 is composed of, for example, a pressure sensor.

 吸入圧力検出部87は、圧縮機16の吸入口側に配置されている。吸入圧力検出部87は、例えば、圧縮機16と第3熱交換器13との間の冷媒配管18に取り付けられている。吸入圧力検出部87は、圧縮機16に吸入される冷媒の圧力を検出する。吸入圧力検出部87は、例えば、圧力センサから構成される。 The suction pressure detector 87 is arranged on the suction port side of the compressor 16 . The suction pressure detector 87 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the third heat exchanger 13 . The suction pressure detector 87 detects the pressure of the refrigerant sucked into the compressor 16 . The suction pressure detection unit 87 is composed of, for example, a pressure sensor.

 吐出温度検出部88は、圧縮機16の吐出口側に配置されている。吐出温度検出部88は、例えば、圧縮機16と第1熱交換器11との間の冷媒配管18に取り付けられている。吐出温度検出部88は、圧縮機16から吐出される冷媒の温度を検出する。吐出温度検出部88は、例えば、温度センサから構成される。 The discharge temperature detector 88 is arranged on the discharge port side of the compressor 16 . The discharge temperature detector 88 is attached, for example, to the refrigerant pipe 18 between the compressor 16 and the first heat exchanger 11 . A discharge temperature detector 88 detects the temperature of the refrigerant discharged from the compressor 16 . The discharge temperature detection unit 88 is composed of, for example, a temperature sensor.

 なお、図1においては、空気調和装置200が冷房運転と除湿運転のみを行う場合の冷媒回路構成を示しているが、その場合に限らず、空気調和装置200は、さらに暖房運転を行うようにしてもよい。図16は、実施の形態1に係る空気調和装置200の変形例である空気調和装置200Aの構成の一例を示す冷媒回路図である。空気調和装置200Aは、冷房運転モードと除湿運転モードと暖房運転モードとを有している。 Although FIG. 1 shows the refrigerant circuit configuration when the air conditioner 200 performs only the cooling operation and the dehumidifying operation, the air conditioner 200 is not limited to that case, and the air conditioner 200 may also perform the heating operation. may FIG. 16 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200A that is a modification of the air conditioner 200 according to Embodiment 1. As shown in FIG. The air conditioner 200A has a cooling operation mode, a dehumidifying operation mode, and a heating operation mode.

 図16に示すように、空気調和装置200Aにおいては、図1の構成に対して、流路切替装置30、第2絞り装置31、および、第4冷媒温度検出部89が追加されている。 As shown in FIG. 16, in the air conditioner 200A, a channel switching device 30, a second expansion device 31, and a fourth refrigerant temperature detection section 89 are added to the configuration of FIG.

 流路切替装置30は、圧縮機16の吐出口と、第1熱交換器11及び第3熱交換器13との間に配置されている。流路切替装置30は、例えば、四方弁から構成されている。流路切替装置30は、空気調和装置200の運転モードが冷房運転モードか暖房運転モードかに応じて、冷媒の流れる方向を切り替える。但し、空気調和装置200Aにおいても、空気調和装置200と同様に、冷房運転モードと除湿運転モードとは、冷媒の流れる方向は同じである。図16において、流路切替装置30の実線は、流路切替装置30の冷房運転モード時の状態を示し、流路切替装置30の破線は、流路切替装置30の暖房運転モード時の状態を示している。つまり、流路切替装置30は、冷房運転モード時においては、圧縮機16の吐出口と第1熱交換器11とを接続すると共に、圧縮機16の吸入口と第3熱交換器13とを接続するように冷媒の流れを切り替える。また、流路切替装置30は、暖房運転モード時においては、圧縮機16の吐出口と第3熱交換器13とを接続すると共に、圧縮機16の吸入口と第1熱交換器11とを接続するように冷媒の流れを切り替える。これにより、冷房運転モード時と暖房運転モード時では、冷媒の流れる方向は逆になる。 The flow switching device 30 is arranged between the discharge port of the compressor 16 and the first heat exchanger 11 and the third heat exchanger 13 . The channel switching device 30 is composed of, for example, a four-way valve. The flow path switching device 30 switches the direction of refrigerant flow depending on whether the operation mode of the air conditioner 200 is the cooling operation mode or the heating operation mode. However, also in the air conditioner 200A, as in the air conditioner 200, the direction in which the refrigerant flows is the same between the cooling operation mode and the dehumidifying operation mode. 16, the solid line of the flow switching device 30 indicates the state of the flow switching device 30 in the cooling operation mode, and the broken line of the flow switching device 30 indicates the state of the flow switching device 30 in the heating operation mode. showing. That is, in the cooling operation mode, the flow switching device 30 connects the discharge port of the compressor 16 and the first heat exchanger 11 and connects the suction port of the compressor 16 and the third heat exchanger 13. Switch refrigerant flow to connect. In the heating operation mode, the flow switching device 30 connects the discharge port of the compressor 16 and the third heat exchanger 13, and connects the suction port of the compressor 16 and the first heat exchanger 11. Switch refrigerant flow to connect. As a result, the direction in which the refrigerant flows is reversed between the cooling operation mode and the heating operation mode.

 冷房運転モードにおいては、圧縮機16から吐出された冷媒は、流路切替装置30を介して、第1熱交換器11に流入される。すなわち、冷房運転モードにおいては、冷媒は、圧縮機16、流路切替装置30、第1熱交換器11、第2絞り装置31、第2熱交換器12、絞り装置17、第3熱交換器13、流路切替装置30、圧縮機16の順に流れる。 In the cooling operation mode, the refrigerant discharged from the compressor 16 flows into the first heat exchanger 11 via the flow switching device 30 . That is, in the cooling operation mode, the refrigerant is the compressor 16, the flow path switching device 30, the first heat exchanger 11, the second expansion device 31, the second heat exchanger 12, the expansion device 17, the third heat exchanger 13, the flow switching device 30, and the compressor 16 in this order.

 一方、暖房運転モードにおいては、圧縮機16から吐出された冷媒は、流路切替装置30を介して、第3熱交換器13に流入される。すなわち、暖房運転モードにおいては、冷媒は、圧縮機16、流路切替装置30、第3熱交換器13、絞り装置17、第2熱交換器12、第2絞り装置31、第1熱交換器11、流路切替装置30、圧縮機16の順に流れる。 On the other hand, in the heating operation mode, the refrigerant discharged from the compressor 16 flows through the flow path switching device 30 into the third heat exchanger 13 . That is, in the heating operation mode, the refrigerant is the compressor 16, the flow path switching device 30, the third heat exchanger 13, the expansion device 17, the second heat exchanger 12, the second expansion device 31, the first heat exchanger 11, the flow switching device 30, and the compressor 16 in this order.

 第2絞り装置31は、第1熱交換器11と第2熱交換器12との間に配置されている。暖房運転モードにおいて、第2絞り装置31は、第2熱交換器12から流出された冷媒を膨張させて減圧する。 The second throttle device 31 is arranged between the first heat exchanger 11 and the second heat exchanger 12 . In the heating operation mode, the second expansion device 31 expands the refrigerant discharged from the second heat exchanger 12 to reduce the pressure.

 第4冷媒温度検出部89は、暖房運転モードにおける冷媒の流れる方向において、第1熱交換器11の下流に配置されている。第4冷媒温度検出部89は、例えば、第1熱交換器11と流路切替装置30との間の冷媒配管18に設けられている。第4冷媒温度検出部89は、暖房運転モードにおいて、第1熱交換器11の出口冷媒温度を検出する。第4冷媒温度検出部89の検出結果は、制御部90に入力される。 The fourth refrigerant temperature detector 89 is arranged downstream of the first heat exchanger 11 in the refrigerant flow direction in the heating operation mode. The fourth refrigerant temperature detector 89 is provided, for example, in the refrigerant pipe 18 between the first heat exchanger 11 and the flow path switching device 30 . The fourth refrigerant temperature detector 89 detects the outlet refrigerant temperature of the first heat exchanger 11 in the heating operation mode. A detection result of the fourth coolant temperature detection unit 89 is input to the control unit 90 .

 このように、図16に示すように、流路切替装置30を追加して、冷房運転モード時と逆方向の冷媒流れを形成可能にし、且つ、第1熱交換器11と第2熱交換器12との間に第2絞り装置31を追加すれば、空気調和装置200が暖房運転を行うことも可能である。 Thus, as shown in FIG. 16, the flow switching device 30 is added to enable the formation of a refrigerant flow in the direction opposite to that in the cooling operation mode, and the first heat exchanger 11 and the second heat exchanger 12, the air conditioner 200 can perform heating operation.

 あるいは、特許文献1に記載のように、空気の流れ方向を切り替えることにより、暖房運転を行うようにしても良い。すなわち、第1熱交換器11が給気経路19内にあり、第2熱交換器12と第3熱交換器13とが還気経路20内にあるように、風路を切り替える切り替え機構を、図1の構成に追加すればよい。 Alternatively, as described in Patent Document 1, heating operation may be performed by switching the air flow direction. That is, the switching mechanism for switching the air passages so that the first heat exchanger 11 is in the air supply passage 19 and the second heat exchanger 12 and the third heat exchanger 13 are in the return air passage 20, It may be added to the configuration of FIG.

 なお、以下では、説明の簡略化のため、図1の冷媒回路の場合を例に挙げて、実施の形態1について説明する。 To simplify the description, the first embodiment will be described below using the refrigerant circuit of FIG. 1 as an example.

 (制御部90)
 図1に示すように、空気調和装置200は、制御部90をさらに備えている。制御部90は、空気調和装置200の全体の動作の制御を行うものであり、例えばアナログ回路、デジタル回路、CPU、または、これらのうちの2つ以上が組み合わされた処理回路で構成されている。処理回路の少なくとも一部分がCPU(プロセッサ)の場合、制御部90の当該一部分の各機能は、ソフトウェア、ファームウェア、または、ソフトウェアとファームウェアとの組み合わせにより実現される。ソフトウェアおよびファームウェアはプログラムとして記述され、メモリに格納される。処理回路は、メモリに記憶されたプログラムを読み出して実行することにより、制御部90の各機能を実現する。ここで、メモリとは、例えば、RAM(Random Access Memory)、ROM(Read Only Memory)、フラッシュメモリ、EPROM(Erasable Programmable ROM)などの不揮発性または揮発性の半導体メモリ、磁気ディスク、フレキシブルディスク、光ディスク、コンパクトディスク、ミニディスク、DVD(Digital Versatile Disc)などが該当する。
(control unit 90)
As shown in FIG. 1 , the air conditioner 200 further includes a controller 90 . The control unit 90 controls the overall operation of the air conditioner 200, and is composed of, for example, an analog circuit, a digital circuit, a CPU, or a processing circuit in which two or more of these are combined. . When at least part of the processing circuit is a CPU (processor), each function of that part of the control unit 90 is implemented by software, firmware, or a combination of software and firmware. Software and firmware are written as programs and stored in memory. The processing circuit implements each function of the control unit 90 by reading and executing the program stored in the memory. Here, the memory means, for example, non-volatile or volatile semiconductor memory such as RAM (Random Access Memory), ROM (Read Only Memory), flash memory, EPROM (Erasable Programmable ROM), magnetic disk, flexible disk, optical disk , compact discs, mini discs, and DVDs (Digital Versatile Discs).

 制御部90は、検出部80~88の検出結果に基づいて、圧縮機16の周波数および絞り装置17の開度等のヒートポンプ回路の動作の制御、並びに、給気ファン14の回転数および還気ファン15の回転数等の空気の流れの制御を行う。検出部80~88の検出結果とは、例えば、上述した、吐出圧力検出部86、吸入圧力検出部87、吐出温度検出部88、第1冷媒温度検出部83、第2冷媒温度検出部84、および、第3冷媒温度検出部85、第1温度湿度検出部80、第2温度湿度検出部81、および、外気温度検出部82の検出結果のうちの少なくとも1つである。 Based on the detection results of the detection units 80 to 88, the control unit 90 controls the operation of the heat pump circuit such as the frequency of the compressor 16 and the opening of the expansion device 17, and the rotation speed of the supply fan 14 and return air. It controls the air flow such as the number of revolutions of the fan 15 . The detection results of the detection units 80 to 88 are, for example, the above-described discharge pressure detection unit 86, suction pressure detection unit 87, discharge temperature detection unit 88, first refrigerant temperature detection unit 83, second refrigerant temperature detection unit 84, and at least one of the detection results of the third refrigerant temperature detection unit 85, the first temperature/humidity detection unit 80, the second temperature/humidity detection unit 81, and the outside air temperature detection unit 82.

 また、制御部90は、リモートコントローラ(図示せず)からの指示に基づいて、圧縮機16の周波数、給気ファン14の回転数、還気ファン15の回転数、絞り装置17の開度等を制御する。 Further, the control unit 90 controls the frequency of the compressor 16, the number of rotations of the supply air fan 14, the number of rotations of the return air fan 15, the opening of the expansion device 17, etc. based on instructions from a remote controller (not shown). to control.

 制御部90の制御により、空気調和装置200において、冷房運転モード又は除湿運転モードにおける運転が実施される。 Under the control of the control unit 90, the air conditioner 200 is operated in the cooling operation mode or the dehumidifying operation mode.

 なお、実施の形態1では、制御部90が空気調和装置200の内部に設けられている場合について示しているが、制御部90は空気調和装置200の外部に設けられていてもよい。また、制御部90は、1つの制御部から構成されていてもよいが、複数の制御部から構成されていてもよい。制御部90が複数の制御部から構成されている場合、そのうちの少なくとも1つが、給気ファン14と還気ファン15などの空気流れに関する制御を行い、他の少なくとも1つが、ヒートポンプ回路の冷媒流れに関する制御を行うようにしてもよい。 Although Embodiment 1 shows the case where the control unit 90 is provided inside the air conditioner 200 , the control unit 90 may be provided outside the air conditioner 200 . Further, the control unit 90 may be composed of one control unit, or may be composed of a plurality of control units. When the control unit 90 is composed of a plurality of control units, at least one of them controls the air flow of the supply air fan 14 and the return air fan 15, and at least one of the other controls the refrigerant flow of the heat pump circuit. may be controlled.

 [空気調和装置200の動作]
 上述したように、実施の形態1に係る空気調和装置200においては、冷房運転モードと除湿運転モードとにおいて、冷媒の流れる方向は同じである。冷房運転モードと除湿運転モードとの違いは、以下の点である。
[Operation of air conditioner 200]
As described above, in the air conditioner 200 according to Embodiment 1, the refrigerant flows in the same direction in the cooling operation mode and the dehumidifying operation mode. The differences between the cooling operation mode and the dehumidifying operation mode are as follows.

 (1)第2熱交換器12が、冷房運転モードにおいては蒸発器として機能し、除湿運転モードにおいては凝縮器として機能する。
 (2)冷房運転モードにおける絞り装置17の開度OPは、除湿運転モードに比べて小さい。
 (3)除湿運転モードにおいて、制御部90は、絞り装置17の開度OPを減少させることにより、第2熱交換器12の外気OAに対する加熱能力を減少させる。また、絞り装置17の開度OPを増加させることにより、第2熱交換器12の外気OAに対する加熱能力を増加させる制御を行う。
(1) The second heat exchanger 12 functions as an evaporator in the cooling operation mode, and functions as a condenser in the dehumidification operation mode.
(2) The opening degree OP of the expansion device 17 in the cooling operation mode is smaller than that in the dehumidification operation mode.
(3) In the dehumidifying operation mode, the controller 90 reduces the opening degree OP of the expansion device 17 to reduce the heating capacity of the second heat exchanger 12 for the outside air OA. Further, by increasing the opening degree OP of the expansion device 17, control is performed to increase the heating capacity of the second heat exchanger 12 for the outside air OA.

 すなわち、実施の形態1においては、空気調和装置200は、上記(1)および(2)により、冷房運転モードと除湿運転モードとにおいて冷媒の流れる方向を切り替える必要がない。制御部90が絞り装置17の開度OPを調整することで、第2熱交換器12が蒸発器として機能するか凝縮器として機能するかが決定される。そのため、除湿運転モードと冷房運転モードとを連続的に移行することができる。また、上記(3)により、制御部90が、絞り装置17の開度OPを調整することで、第2熱交換器12の加熱能力が調整できる。これにより、除湿運転モードにおける運転において、室内300の温度低下を抑制しながら、室内300の湿度を低下させる除湿運転が可能となる。以下に詳細に説明する。 That is, in Embodiment 1, the air conditioner 200 does not need to switch the direction of refrigerant flow between the cooling operation mode and the dehumidifying operation mode due to the above (1) and (2). The controller 90 adjusts the opening degree OP of the expansion device 17 to determine whether the second heat exchanger 12 functions as an evaporator or a condenser. Therefore, it is possible to continuously transition between the dehumidifying operation mode and the cooling operation mode. Further, according to (3) above, the control unit 90 adjusts the opening degree OP of the expansion device 17, so that the heating capacity of the second heat exchanger 12 can be adjusted. As a result, in the operation in the dehumidifying operation mode, the dehumidifying operation that reduces the humidity in the room 300 while suppressing the temperature drop in the room 300 becomes possible. Details will be described below.

 以下、空気調和装置200の動作について、冷媒の流れおよび空気の流れと共に説明する。 The operation of the air conditioner 200 will be described below together with the refrigerant flow and the air flow.

 <冷房運転>
 まず、空気調和装置200が実行する動作のうち、冷房運転について図1~図3を用いて説明する。冷房運転においては、空気調和装置200は、室外301の空気を降温して室内300に給気する。図2は、実施の形態1に係る空気調和装置200の冷房運転モードにおける冷媒の流れおよび空気の流れを説明する説明図である。図3は、実施の形態1に係る空気調和装置200の冷房運転モードにおける冷媒状態を示すモリエル線図である。なお、図2では、冷媒の流れる方向を実線の矢印で示し、空気の流れる方向を破線の矢印で示すと共に、代表的な条件での冷媒および空気の温度の例を矢印に付記している。また、図3において、横軸は冷媒のエンタルピ、縦軸は冷媒の圧力を示している。図3では、空気の温度、および、冷媒の圧力、エンタルピ、冷媒の温度を示している。図3では、破線の曲線により、飽和蒸気線40と飽和液線41とを示している。飽和蒸気線40と飽和液線41との境界は、臨界点Kである。なお、図3において、実際には、状態R2の圧力と状態R2-1の圧力とは同じであるが、図示の便宜上、オーバーラップさせずに、シフトさせて別々に示している。ここでは、熱交換動作において、熱交換流体が空気であり、被熱交換流体が冷媒である場合を例に、空気調和装置200の動作について説明する。
<Cooling operation>
First, among the operations performed by the air conditioner 200, the cooling operation will be described with reference to FIGS. 1 to 3. FIG. In the cooling operation, the air conditioner 200 lowers the temperature of the outdoor air 301 and supplies the indoor 300 with the air. FIG. 2 is an explanatory diagram illustrating the flow of refrigerant and the flow of air in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1. FIG. FIG. 3 is a Mollier diagram showing refrigerant states in the cooling operation mode of the air-conditioning apparatus 200 according to Embodiment 1. FIG. In FIG. 2 , solid line arrows indicate the direction in which the refrigerant flows, dashed line arrows indicate the direction in which air flows, and examples of temperatures of the refrigerant and air under typical conditions are appended to the arrows. In FIG. 3, the horizontal axis indicates the enthalpy of the refrigerant, and the vertical axis indicates the pressure of the refrigerant. FIG. 3 shows air temperature, refrigerant pressure, enthalpy, and refrigerant temperature. In FIG. 3, the saturated vapor line 40 and the saturated liquid line 41 are indicated by dashed curves. A critical point K is the boundary between the saturated vapor line 40 and the saturated liquid line 41 . In FIG. 3, the pressure in the state R2 and the pressure in the state R2-1 are actually the same, but for the convenience of illustration, they are not overlapped and shown separately. Here, in the heat exchange operation, the operation of the air conditioner 200 will be described by taking as an example a case where the heat exchange fluid is air and the heat exchange fluid is refrigerant.

 冷房運転モードにおいては、第1熱交換器11が凝縮器として作用し、第2熱交換器12および第3熱交換器13が蒸発器として作用する。 In the cooling operation mode, the first heat exchanger 11 acts as a condenser, and the second heat exchanger 12 and the third heat exchanger 13 act as evaporators.

 図2および図3に示すように、圧縮機16を駆動させることによって、圧縮機16から高温高圧のガス状態の冷媒が吐出する(図3の状態R1)。このときの冷媒の温度は、例えば、70℃である。圧縮機16から吐出した高温高圧のガス冷媒(単相)は、凝縮器として機能する第1熱交換器11に流れ込む。第1熱交換器11では、流れ込んだ高温高圧のガス冷媒と、還気ファン15によって室内300から室外301へ還気される還気RAとの間で熱交換が行われる。還気RAの温度Tは、例えば、27℃である。その結果、高温高圧のガス冷媒が凝縮して、高圧の液冷媒(単相)になる(図3の状態R2)。冷房運転においては、除湿運転時よりも、絞り装置17の開度OPを小さく設定している。これにより、状態R2における冷媒の圧力Pを値P1まで上昇させ、熱交換を促進することで、第1熱交換器11から流出する液冷媒の温度を、還気RAの温度Tと同程度まで低下させることができる。第1熱交換器11から流出される冷媒の温度は、例えば、27℃である。このように、絞り装置17の開度OPは、制御部90の制御により、後述する除湿運転モードに比べて小さくなるように設定される。なお、値P1は、図6に示す除湿運転時の値P2以上の値である。 As shown in FIGS. 2 and 3, by driving the compressor 16, high-temperature and high-pressure gaseous refrigerant is discharged from the compressor 16 (state R1 in FIG. 3). The temperature of the coolant at this time is, for example, 70°C. The high-temperature and high-pressure gas refrigerant (single-phase) discharged from the compressor 16 flows into the first heat exchanger 11 functioning as a condenser. In the first heat exchanger 11 , heat is exchanged between the high-temperature, high-pressure gas refrigerant that has flowed in and the return air RA that is returned from the room 300 to the outside 301 by the return air fan 15 . The temperature TR of the return air RA is, for example, 27°C. As a result, the high-temperature and high-pressure gas refrigerant is condensed into a high-pressure liquid refrigerant (single-phase) (state R2 in FIG. 3). In the cooling operation, the opening degree OP of the expansion device 17 is set smaller than that in the dehumidifying operation. As a result, the pressure P of the refrigerant in the state R2 is increased to the value P1 to promote heat exchange, so that the temperature of the liquid refrigerant flowing out of the first heat exchanger 11 is made approximately the same as the temperature TR of the return air RA. can be lowered to The temperature of the refrigerant flowing out of the first heat exchanger 11 is, for example, 27°C. Thus, the opening degree OP of the expansion device 17 is set by the control of the control unit 90 so as to be smaller than that in the dehumidifying operation mode, which will be described later. Note that the value P1 is a value equal to or greater than the value P2 during the dehumidifying operation shown in FIG.

 第1熱交換器11から送り出された高圧の液冷媒は、蒸発器として機能する第2熱交換器12において、外気OAと熱交換し、蒸発する(図3の状態R3)。ここで、室内300の温度は、空気調和装置200または他の空気調和装置によって、外気OAよりも低温に調整されているため、還気RAの温度Tは外気OAの温度Toよりも低い。例えば、還気RAの温度Tが27℃で、外気OAの温度Tが35℃である。第1熱交換器11から第2熱交換器12に流入される液冷媒の温度は、上述したように、還気RAの温度Tと同程度であり、外気OAよりも低い。従って、外気OAは、第2熱交換器12の熱交換において冷却される。従って、第2熱交換器12を通過した外気OAの温度T1は、例えば、27℃である。第2熱交換器12で蒸発して昇温された液冷媒は、絞り装置17によって低圧のガス冷媒と液冷媒との二相状態の冷媒になる(図3の状態R4)。二相状態の冷媒は、蒸発器として機能する第3熱交換器13に流れ込む。第3熱交換器13では、流れ込んだ二相状態の冷媒と、給気ファン14によって室外301から室内300へ供給される外気OAとの間で熱交換が行われる。その結果、二相状態の冷媒のうち液冷媒が蒸発して、低圧のガス冷媒(単相)になる(図3の状態R5)。第3熱交換器13において、外気OAは冷却される。第3熱交換器13を通過した外気OAの温度T2は、例えば、15℃である。給気経路19では、図2に示すように、第2熱交換器12を通過した空気と第3熱交換器13を通過した空気とが混ざり合って、給気SAとなって、室内300に供給される。第3熱交換器13から送り出された低圧のガス冷媒は、圧縮機16に流れ込み、圧縮されて高温高圧のガス冷媒となって、再び圧縮機16から吐出する(図3の状態R1)。以下、このサイクルが繰り返される。 The high-pressure liquid refrigerant sent out from the first heat exchanger 11 exchanges heat with the outside air OA and evaporates in the second heat exchanger 12 functioning as an evaporator (state R3 in FIG. 3). Here, since the temperature of the room 300 is adjusted to be lower than the outside air OA by the air conditioner 200 or another air conditioner, the temperature TR of the return air RA is lower than the temperature To of the outside air OA. For example, the temperature T R of the return air RA is 27°C and the temperature T O of the outside air OA is 35°C. The temperature of the liquid refrigerant flowing from the first heat exchanger 11 to the second heat exchanger 12 is approximately the same as the temperature TR of the return air RA and lower than the outside air OA, as described above. Therefore, the outside air OA is cooled in the heat exchange of the second heat exchanger 12 . Therefore, the temperature T O 1 of the outside air OA that has passed through the second heat exchanger 12 is, for example, 27°C. The liquid refrigerant evaporated and heated in the second heat exchanger 12 becomes a two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant by the throttle device 17 (state R4 in FIG. 3). The two-phase refrigerant flows into the third heat exchanger 13 functioning as an evaporator. In the third heat exchanger 13 , heat is exchanged between the flowing two-phase refrigerant and the outside air OA supplied from the outdoor 301 to the indoor 300 by the air supply fan 14 . As a result, the liquid refrigerant of the two-phase refrigerant evaporates to become a low-pressure gas refrigerant (single-phase) (state R5 in FIG. 3). The outside air OA is cooled in the third heat exchanger 13 . The temperature T O 2 of the outside air OA that has passed through the third heat exchanger 13 is, for example, 15°C. In the air supply path 19, as shown in FIG. 2, the air that has passed through the second heat exchanger 12 and the air that has passed through the third heat exchanger 13 are mixed to form supply air SA, which is supplied to the room 300. supplied. The low-pressure gas refrigerant sent out from the third heat exchanger 13 flows into the compressor 16, is compressed into high-temperature and high-pressure gas refrigerant, and is discharged from the compressor 16 again (state R1 in FIG. 3). This cycle is then repeated.

 (冷房運転時の制御部90の動作)
 冷房運転モードにおける制御部90の働きについて説明する。制御部90は、圧縮機16の吐出冷媒圧力と、第1熱交換器11の出口冷媒温度とに基づいて、室内300の温度が設定温度になるように、絞り装置17の開度OPを制御する。
(Operation of control unit 90 during cooling operation)
The function of the control unit 90 in the cooling operation mode will be described. The control unit 90 controls the opening degree OP of the expansion device 17 based on the discharge refrigerant pressure of the compressor 16 and the outlet refrigerant temperature of the first heat exchanger 11 so that the temperature in the room 300 reaches the set temperature. do.

 図4は、実施の形態1に係る空気調和装置200における冷房運転モード時の制御部90の動作を示すフローチャートである。ステップS1で、制御部90は、吐出圧力検出部86から、圧縮機16の吐出口側の冷媒圧力を取得する。次に、ステップS2で、制御部90は、取得した冷媒圧力に基づいて、当該圧力における飽和温度を算出する。次に、ステップS3で、制御部90は、第1冷媒温度検出部83から、第1熱交換器11の出口冷媒温度を取得する。次に、ステップS4で、制御部90は、ステップS2で算出した飽和温度と、ステップS3で取得した出口冷媒温度とに基づいて、第1熱交換器11の出口過冷却度SC1を算出する。制御部90は、算出した出口過冷却度SC1を指標として、絞り装置17の開度OPを制御する。具体的には、制御部90は、ステップS5で、出口過冷却度SC1と、閾値Th1とを比較する。出口過冷却度SC1が閾値Th1より大きい場合は、ステップS6の処理に進み、出口過冷却度SC1が閾値Th1以下の場合は、ステップS7の処理に進む。ステップS6では、制御部90は、絞り装置17の開度OPを現在の値より増加させる。一方、ステップS7では、制御部90は、絞り装置17の開度OPを現在の値より減少させる。なお、絞り装置17の開度OPの増減量は、予め設定された一定値にしてもよいが、制御部90が、出口過冷却度SC1と閾値Th1との差分に応じて増減量を決定するようにしてもよい。 FIG. 4 is a flow chart showing the operation of the control unit 90 in the cooling operation mode of the air conditioner 200 according to Embodiment 1. FIG. In step S<b>1 , the control unit 90 acquires the refrigerant pressure on the discharge port side of the compressor 16 from the discharge pressure detection unit 86 . Next, in step S2, based on the acquired refrigerant pressure, the control unit 90 calculates the saturation temperature at that pressure. Next, in step S<b>3 , the control unit 90 acquires the outlet refrigerant temperature of the first heat exchanger 11 from the first refrigerant temperature detection unit 83 . Next, in step S4, the control unit 90 calculates the degree of supercooling SC1 at the outlet of the first heat exchanger 11 based on the saturation temperature calculated in step S2 and the outlet refrigerant temperature obtained in step S3. The control unit 90 controls the opening degree OP of the expansion device 17 using the calculated outlet supercooling degree SC1 as an index. Specifically, in step S5, the controller 90 compares the outlet supercooling degree SC1 with the threshold value Th1. When the outlet supercooling degree SC1 is greater than the threshold Th1, the process proceeds to step S6, and when the outlet supercooling degree SC1 is equal to or less than the threshold Th1, the process proceeds to step S7. In step S6, the control unit 90 increases the opening degree OP of the diaphragm device 17 from the current value. On the other hand, in step S7, the controller 90 reduces the opening degree OP of the diaphragm device 17 from the current value. The amount of increase or decrease in the opening degree OP of the expansion device 17 may be set to a preset constant value, but the control unit 90 determines the amount of increase or decrease according to the difference between the outlet supercooling degree SC1 and the threshold value Th1. You may do so.

 なお、閾値Th1は、通常の冷房運転を想定した第1熱交換器11の出口過冷却度の設計値(すなわち、通常運転時の理論値)に基づいて予め設定した固定値であってもよいが、可変の値でもよい。その場合、例えば、閾値Th1は、制御部90によって、空気調和装置200に対してユーザーから設定される室内300の室温に対する設定値に基づいて決定される。なお、決定方法としては、データテーブルまたは演算式をメモリに予め格納しておき、制御部90が、それを用いて閾値Th1を演算する。当該データテーブルには、室温に対する設定値ごとに、閾値Th1を記憶しておく。また、演算式は、室温に対する設定値をパラメータとして閾値Th1を求める関数である。 Note that the threshold Th1 may be a fixed value set in advance based on the design value of the degree of subcooling at the outlet of the first heat exchanger 11 assuming normal cooling operation (that is, the theoretical value during normal operation). can be a variable value. In that case, for example, the threshold Th1 is determined by the controller 90 based on the set value for the room temperature of the room 300 set by the user for the air conditioner 200 . As a determination method, a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th1. The data table stores a threshold value Th1 for each set value for room temperature. Moreover, the arithmetic expression is a function for obtaining the threshold value Th1 using the set value for the room temperature as a parameter.

 なお、冷房運転モードにおける絞り装置17の開度OPは、除湿運転モードに比べて小さい値に設定される。具体的に説明する。冷房運転モードにおける絞り装置17の開度OPと除湿運転モードにおける絞り装置17の開度OPとの間の境界値を境界点OP(図8参照)とする。このとき、冷房運転モードにおける絞り装置17の開度OPは、境界点OP以下の第1範囲内の値であり、除湿運転モードにおける絞り装置17の開度OPは、境界点OPより大きい第2範囲内の値である。 Note that the opening degree OP of the expansion device 17 in the cooling operation mode is set to a smaller value than in the dehumidification operation mode. A specific description will be given. A boundary value between the opening degree OP of the expansion device 17 in the cooling operation mode and the opening degree OP of the expansion device 17 in the dehumidifying operation mode is defined as a boundary point OP A (see FIG. 8). At this time, the opening degree OP of the expansion device 17 in the cooling operation mode is a value within the first range below the boundary point OP A , and the opening degree OP of the expansion device 17 in the dehumidifying operation mode is greater than the boundary point OP A. A value within the second range.

 また、冷房運転モードにおいて、制御部90は、以下のような制御を実施してもよい。給気ファン14の回転数、および、還気ファン15の回転数は、室内300の必要換気量に応じて、予め決定されるものである。ただし、空気調和装置200のほかに換気装置が設けられているなどの理由で、給気ファン14および還気ファン15の回転数を変更できる場合が想定される。その場合には、制御部90が、給気ファン14および還気ファン15の回転数を上昇させることにより、出口過冷却度SC1を増加させ、給気ファン14および還気ファン15の回転数を低下させることにより、出口過冷却度SC1を減少させるようにしてもよい。 Also, in the cooling operation mode, the control unit 90 may perform the following control. The number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 are determined in advance according to the required ventilation amount of the room 300 . However, it is assumed that the rotation speeds of the supply air fan 14 and the return air fan 15 can be changed, for example, because a ventilator is provided in addition to the air conditioner 200 . In that case, the control unit 90 increases the outlet supercooling degree SC1 by increasing the rotation speeds of the supply air fan 14 and the return air fan 15, and increases the rotation speeds of the supply air fan 14 and the return air fan 15. By decreasing, the outlet supercooling degree SC1 may be decreased.

 また、制御部90は、圧縮機16の吸入圧力と、第3熱交換器13の出口冷媒温度とに基づいて、絞り装置17の開度OPを制御するようにしてもよい。その場合、制御部90は、吸入圧力検出部87から、圧縮機16が吸入する冷媒の圧力を取得して、当該圧力における飽和温度を算出する。また、制御部90は、第3冷媒温度検出部85から、第3熱交換器13の出口冷媒温度を取得する。制御部90は、算出した飽和温度と取得した出口冷媒温度とに基づいて、第3熱交換器13の出口過熱度SHeを算出する。制御部90は、出口過熱度SHeが、予め設定された閾値Th2以下のとき、圧縮機16への液吸入を防止するために、絞り装置17の開度OPを減少させる制御を実施する。一方、制御部90は、出口過熱度SHeが閾値Th2より大きい場合には、絞り装置17の開度OPを現在の値に維持する。 Also, the control unit 90 may control the opening degree OP of the expansion device 17 based on the suction pressure of the compressor 16 and the outlet refrigerant temperature of the third heat exchanger 13 . In this case, the controller 90 acquires the pressure of the refrigerant sucked by the compressor 16 from the suction pressure detector 87 and calculates the saturation temperature at that pressure. The control unit 90 also acquires the outlet refrigerant temperature of the third heat exchanger 13 from the third refrigerant temperature detection unit 85 . The control unit 90 calculates the outlet superheat degree SHe of the third heat exchanger 13 based on the calculated saturation temperature and the acquired outlet refrigerant temperature. When the outlet superheat degree SHe is equal to or less than a preset threshold value Th2, the control unit 90 performs control to decrease the opening degree OP of the expansion device 17 in order to prevent the liquid from being sucked into the compressor 16 . On the other hand, when the outlet superheat degree SHe is greater than the threshold value Th2, the control unit 90 maintains the opening degree OP of the expansion device 17 at the current value.

 また、制御部90は、圧縮機16の吐出圧力と、圧縮機16の吐出冷媒温度とに基づいて、絞り装置17の開度OPを制御するようにしてもよい。その場合、制御部90は、吐出圧力検出部86から、圧縮機16が吐出する冷媒の圧力を取得して、当該圧力における飽和温度を算出する。また、制御部90は、吐出温度検出部88から、圧縮機16が吐出する冷媒の温度を取得する。制御部90は、算出した飽和温度と取得した冷媒の温度とに基づいて、圧縮機16の吐出過熱度SHdを算出する。制御部90は、予め設定された吐出温度の閾値Th3-1と、吐出過熱度SHdの閾値Th3-2に応じて絞り装置17の開度OPを制御する。吐出温度検出部88が閾値Th3-1以上の場合は、絞り装置17の開度OPを増加させる制御を実施する。これにより、蒸発器として機能する第3熱交換器13の出口冷媒を湿り状態にして、圧縮機16に微量の液冷媒を吸入させ、圧縮機16の吐出温度を低下させる。吐出温度検出部88が閾値Th3-1未満の場合は、絞り装置17の開度OPを現在の値に維持する。吐出過熱度SHdが閾値Th3-2以下の場合は、絞り装置17の開度OPを減少させる制御を実施する。これにより、圧縮機16への過剰な液流入を防止することができる。吐出過熱度SHdが閾値Th3-2より大きい場合は、絞り装置17の開度OPを現在の値に維持する。 Also, the control unit 90 may control the opening degree OP of the expansion device 17 based on the discharge pressure of the compressor 16 and the temperature of the refrigerant discharged from the compressor 16 . In that case, the control unit 90 acquires the pressure of the refrigerant discharged from the compressor 16 from the discharge pressure detection unit 86 and calculates the saturation temperature at that pressure. The control unit 90 also acquires the temperature of the refrigerant discharged from the compressor 16 from the discharge temperature detection unit 88 . The control unit 90 calculates the degree of discharge superheat SHd of the compressor 16 based on the calculated saturation temperature and the acquired temperature of the refrigerant. The control unit 90 controls the opening degree OP of the throttle device 17 according to the preset threshold value Th3-1 of the ejection temperature and the threshold value Th3-2 of the ejection superheat degree SHd. When the ejection temperature detection unit 88 is equal to or higher than the threshold value Th3-1, control is performed to increase the opening degree OP of the expansion device 17 . As a result, the refrigerant at the outlet of the third heat exchanger 13 functioning as an evaporator is brought into a wet state, causing the compressor 16 to suck in a small amount of liquid refrigerant, thereby lowering the discharge temperature of the compressor 16 . When the discharge temperature detection unit 88 is less than the threshold value Th3-1, the opening degree OP of the expansion device 17 is maintained at the current value. When the degree of discharge superheat SHd is equal to or less than the threshold value Th3-2, control is performed to decrease the degree of opening OP of the throttle device 17 . As a result, excessive inflow of liquid into the compressor 16 can be prevented. When the discharge superheat SHd is greater than the threshold value Th3-2, the opening OP of the expansion device 17 is maintained at the current value.

 <除湿運転>
 次に、空気調和装置200が実行する運転のうち、除湿運転について、図1、図5、図6を用いて説明する。除湿運転では、空気調和装置200は、室外301の空気を室内300に除湿して給気する。図5は、実施の形態1に係る空気調和装置200の除湿運転モードにおける冷媒の流れおよび空気の流れを説明する説明図である。図6は、実施の形態1に係る空気調和装置200の除湿運転モードにおける冷媒状態を示すモリエル線図である。なお、図5では、冷媒の流れる方向を実線の矢印で示し、空気の流れる方向を破線の矢印で示し、また、代表的な条件での冷媒および空気の温度を矢印に付記している。図6において、横軸は冷媒のエンタルピ、縦軸は冷媒の圧力を示している。図6では、空気の温度、および、冷媒の圧力、エンタルピ、冷媒の温度を示している。また、図6では、破線の曲線により、飽和蒸気線40と飽和液線41とを示している。飽和蒸気線40と飽和液線41との境界は、臨界点Kである。ここでは、熱交換流体が空気であり、被熱交換流体が冷媒である場合を例に、空気調和装置200の動作について説明する。
<Dehumidification operation>
Next, among the operations performed by the air conditioner 200, the dehumidification operation will be described with reference to FIGS. 1, 5, and 6. FIG. In the dehumidifying operation, the air conditioner 200 dehumidifies the outdoor air 301 and supplies the indoor air 300 with the dehumidified air. FIG. 5 is an explanatory diagram illustrating the refrigerant flow and the air flow in the dehumidifying operation mode of the air conditioner 200 according to Embodiment 1. FIG. FIG. 6 is a Mollier diagram showing refrigerant states in the dehumidifying operation mode of the air-conditioning apparatus 200 according to Embodiment 1. FIG. In FIG. 5 , solid line arrows indicate the direction of refrigerant flow, broken line arrows indicate the direction of air flow, and the temperatures of the refrigerant and air under typical conditions are appended to the arrows. In FIG. 6, the horizontal axis indicates the enthalpy of the refrigerant, and the vertical axis indicates the pressure of the refrigerant. FIG. 6 shows air temperature, refrigerant pressure, enthalpy, and refrigerant temperature. Further, in FIG. 6, the saturated vapor line 40 and the saturated liquid line 41 are indicated by dashed curved lines. A critical point K is the boundary between the saturated vapor line 40 and the saturated liquid line 41 . Here, the operation of the air conditioner 200 will be described by taking as an example a case where the heat exchange fluid is air and the heat exchange fluid is refrigerant.

 除湿運転モードにおいては、第1熱交換器11および第2熱交換器12が凝縮器として作用し、第3熱交換器13が蒸発器として作用する。 In the dehumidifying operation mode, the first heat exchanger 11 and the second heat exchanger 12 act as condensers, and the third heat exchanger 13 acts as an evaporator.

 図5および図6に示すように、圧縮機16を駆動させることによって圧縮機16から高温高圧のガス状態の冷媒が吐出する。圧縮機16から吐出した高温高圧のガス冷媒(単相)は、凝縮器として機能する第1熱交換器11に流れ込む(図6の状態R1)。第1熱交換器11では、流れ込んだ高温高圧のガス冷媒と、還気ファン15によって室内300から室外301へ排気される還気RAとの間で熱交換が行われ、高温高圧のガス冷媒が凝縮して高圧の液冷媒または二相冷媒になる(図6の状態R2)。このとき、除湿運転モードにおいては、制御部90が、絞り装置17の開度OPを冷房運転モードに比べて大きくすることにより、状態R2の圧力Pを冷房運転モード時の値P1よりも低い値P2にする。こうして熱交換を抑制することにより、液冷媒の温度を外気OAの温度Tより高い温度まで低下させる。第1熱交換器11から送り出された液冷媒の温度は、例えば45℃で、外気OAの温度は、例えば35℃である。 As shown in FIGS. 5 and 6, when the compressor 16 is driven, a high-temperature, high-pressure gaseous refrigerant is discharged from the compressor 16 . The high-temperature and high-pressure gas refrigerant (single-phase) discharged from the compressor 16 flows into the first heat exchanger 11 functioning as a condenser (state R1 in FIG. 6). In the first heat exchanger 11, heat is exchanged between the high-temperature and high-pressure gas refrigerant that has flowed in and the return air RA that is exhausted from the room 300 to the outside 301 by the return-air fan 15, so that the high-temperature and high-pressure gas refrigerant is It condenses into a high-pressure liquid refrigerant or two-phase refrigerant (state R2 in FIG. 6). At this time, in the dehumidifying operation mode, the control unit 90 increases the opening degree OP of the expansion device 17 compared to that in the cooling operation mode, thereby setting the pressure P in the state R2 to a value lower than the value P1 in the cooling operation mode. Make it P2. By suppressing heat exchange in this manner, the temperature of the liquid refrigerant is lowered to a temperature higher than the temperature TO of the outside air OA. The temperature of the liquid refrigerant sent out from the first heat exchanger 11 is, for example, 45°C, and the temperature of the outside air OA is, for example, 35°C.

 第1熱交換器11から送り出された高圧の液冷媒は、凝縮器として機能する第2熱交換器12に流入される。第2熱交換器12では、当該液冷媒が外気OAと熱交換して凝縮する(図6の状態R3)。このとき、第1熱交換器11から第2熱交換器12に流入した液冷媒の温度(例えば45℃)は、上述したように、外気OAの温度(例えば35℃)より高い。従って、第2熱交換器12において、外気OAは加熱される。第2熱交換器12を通過した外気OAの温度T1は、例えば、45℃である。凝縮した液冷媒は、絞り装置17によって減圧され、低圧のガス冷媒と液冷媒との二相状態の冷媒になる(図6の状態R4)。二相状態の冷媒は、蒸発器として機能する第3熱交換器13に流れ込む。第3熱交換器13では、流れ込んだ二相状態の冷媒と、給気ファン14によって室外301から供給された外気OAとの間で、熱交換が行われて、二相状態の冷媒のうち液冷媒が蒸発して低圧のガス冷媒(単相)になる(図6の状態R5)。第3熱交換器13を通過した外気OAの温度T2は、例えば、15℃である。第3熱交換器13から送り出された低圧のガス冷媒は、圧縮機16に流れ込み、圧縮されて高温高圧のガス冷媒となって、再び圧縮機16から吐出する(図6の状態R1)。以下、このサイクルが繰り返される。 The high-pressure liquid refrigerant sent out from the first heat exchanger 11 flows into the second heat exchanger 12 functioning as a condenser. In the second heat exchanger 12, the liquid refrigerant exchanges heat with the outside air OA and condenses (state R3 in FIG. 6). At this time, the temperature (eg, 45° C.) of the liquid refrigerant flowing from the first heat exchanger 11 to the second heat exchanger 12 is higher than the temperature (eg, 35° C.) of the outside air OA, as described above. Therefore, the outside air OA is heated in the second heat exchanger 12 . The temperature T O 1 of the outside air OA that has passed through the second heat exchanger 12 is, for example, 45°C. The condensed liquid refrigerant is depressurized by the expansion device 17 and becomes two-phase refrigerant of low-pressure gas refrigerant and liquid refrigerant (state R4 in FIG. 6). The two-phase refrigerant flows into the third heat exchanger 13 functioning as an evaporator. In the third heat exchanger 13, heat is exchanged between the flowing two-phase refrigerant and the outside air OA supplied from the outdoor 301 by the air supply fan 14. The refrigerant evaporates and becomes a low-pressure gas refrigerant (single-phase) (state R5 in FIG. 6). The temperature T O 2 of the outside air OA that has passed through the third heat exchanger 13 is, for example, 15°C. The low-pressure gas refrigerant sent out from the third heat exchanger 13 flows into the compressor 16, is compressed into high-temperature and high-pressure gas refrigerant, and is discharged from the compressor 16 again (state R1 in FIG. 6). This cycle is then repeated.

 除湿運転モードでは、第2熱交換器12で加熱された空気と、第3熱交換器13で冷却および除湿された空気とが混合されて給気SAとなって室内300に供給される。これにより、室内300の温度低下を抑制しながら、室内300の湿度を低下させる除湿運転が可能となる。 In the dehumidifying operation mode, the air heated by the second heat exchanger 12 and the air cooled and dehumidified by the third heat exchanger 13 are mixed and supplied to the room 300 as supply air SA. As a result, dehumidifying operation that reduces the humidity in the room 300 while suppressing a temperature drop in the room 300 is possible.

 (除湿運転時の制御部90の動作)
 除湿運転モードにおける制御部90の働きについて説明する。制御部90は、圧縮機16の吐出冷媒圧力と、第2熱交換器12の出口冷媒温度とに基づいて、室内300の温度が設定温度になるように、絞り装置17の開度OPを制御する。絞り装置17の開度OPを制御することにより、第2熱交換器12の加熱能力が増加または減少されるため、第2熱交換器12で加熱されて室内300に供給される空気の温度を調整することができる。これにより、室内300の温度を設定温度に維持することができる。
(Operation of control unit 90 during dehumidification operation)
The operation of the control section 90 in the dehumidifying operation mode will be described. The control unit 90 controls the opening degree OP of the expansion device 17 based on the discharge refrigerant pressure of the compressor 16 and the outlet refrigerant temperature of the second heat exchanger 12 so that the temperature in the room 300 reaches the set temperature. do. By controlling the opening degree OP of the expansion device 17, the heating capacity of the second heat exchanger 12 is increased or decreased, so that the temperature of the air heated by the second heat exchanger 12 and supplied to the room 300 is can be adjusted. Thereby, the temperature in the room 300 can be maintained at the set temperature.

 図7は、実施の形態1に係る空気調和装置200における除湿運転モード時の制御部90の動作を示すフローチャートである。ステップS11で、制御部90は、吐出圧力検出部86から、圧縮機16の吐出口側の冷媒圧力を取得する。次に、ステップS12で、制御部90は、取得した冷媒圧力に基づいて、当該圧力における飽和温度を算出する。次に、ステップS13で、制御部90は、第2冷媒温度検出部84から、第2熱交換器12の出口冷媒温度を取得する。次に、ステップS14で、制御部90は、ステップS12で算出した飽和温度と、ステップS13で取得した冷媒温度とに基づいて、第2熱交換器12の出口過冷却度SC2を算出する。制御部90は、算出した出口過冷却度SC2を指標として、絞り装置17の開度OPを制御する。具体的には、制御部90は、ステップS15で、出口過冷却度SC2と、閾値Th4とを比較する。出口過冷却度SC2が閾値Th4より大きい場合は、ステップS16の処理に進み、出口過冷却度SC2が閾値Th4以下の場合は、ステップS17の処理に進む。ステップS16では、制御部90は、室内300の室温が低下していると判定し、絞り装置17の開度OPを現在の値より増加させる。これにより、第2熱交換器12の加熱能力が増加し、第2熱交換器12を通過した外気OAの温度が高くなる。一方、ステップS17では、制御部90は、室内300の室温が高いと判定し、絞り装置17の開度OPを現在の値より減少させる。これにより、第2熱交換器12の加熱能力が減少し、第2熱交換器12を通過した外気OAの温度が低くなる。なお、絞り装置17の開度OPの増減量は、予め設定された一定値にしてもよいが、制御部90が、出口過冷却度SC2と閾値Th4との差分に応じて増減量を決定するようにしてもよい。 FIG. 7 is a flowchart showing the operation of the control unit 90 in the dehumidifying operation mode in the air conditioner 200 according to Embodiment 1. FIG. In step S<b>11 , the control unit 90 acquires the refrigerant pressure on the discharge port side of the compressor 16 from the discharge pressure detection unit 86 . Next, in step S12, the control unit 90 calculates the saturation temperature at the obtained pressure based on the obtained refrigerant pressure. Next, in step S<b>13 , the control unit 90 acquires the outlet refrigerant temperature of the second heat exchanger 12 from the second refrigerant temperature detection unit 84 . Next, in step S14, the control unit 90 calculates the outlet subcooling degree SC2 of the second heat exchanger 12 based on the saturation temperature calculated in step S12 and the refrigerant temperature obtained in step S13. The control unit 90 controls the opening degree OP of the expansion device 17 using the calculated outlet supercooling degree SC2 as an index. Specifically, in step S15, the controller 90 compares the outlet supercooling degree SC2 with the threshold value Th4. When the outlet supercooling degree SC2 is greater than the threshold Th4, the process proceeds to step S16, and when the outlet supercooling degree SC2 is equal to or less than the threshold Th4, the process proceeds to step S17. In step S16, the control unit 90 determines that the room temperature in the room 300 has decreased, and increases the opening degree OP of the expansion device 17 from the current value. As a result, the heating capacity of the second heat exchanger 12 increases, and the temperature of the outside air OA that has passed through the second heat exchanger 12 rises. On the other hand, in step S17, the controller 90 determines that the room temperature in the room 300 is high, and reduces the opening degree OP of the expansion device 17 from the current value. As a result, the heating capacity of the second heat exchanger 12 is reduced, and the temperature of the outside air OA that has passed through the second heat exchanger 12 is lowered. The amount of increase or decrease in the opening degree OP of the expansion device 17 may be set to a preset constant value, but the control unit 90 determines the amount of increase or decrease according to the difference between the outlet supercooling degree SC2 and the threshold value Th4. You may do so.

 なお、閾値Th4は、通常の除湿運転を想定した第2熱交換器12の出口過冷却度の設計値(すなわち、通常運転時の理論値)に基づいて予め設定した固定値であってもよいが、可変の値でもよい。その場合、例えば、閾値Th4は、制御部90によって、空気調和装置200に対してユーザーから設定される室内300の室温に対する設定値に基づいて決定される。なお、決定方法としては、データテーブルまたは演算式をメモリに予め格納しておき、制御部90が、それを用いて閾値Th4を演算する。当該データテーブルには、室温に対する設定値ごとに、閾値Th4を記憶しておく。また、演算式は、室温に対する設定値をパラメータとして閾値Th4を求める関数である。 Note that the threshold Th4 may be a fixed value set in advance based on the design value of the degree of subcooling at the outlet of the second heat exchanger 12 assuming normal dehumidifying operation (that is, the theoretical value during normal operation). can be a variable value. In that case, for example, the threshold Th4 is determined by the control unit 90 based on the set value for the room temperature of the room 300 set by the user for the air conditioner 200 . As a determination method, a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th4. The data table stores a threshold value Th4 for each set value for room temperature. Moreover, the arithmetic expression is a function for obtaining the threshold value Th4 using the set value for the room temperature as a parameter.

 実施の形態1では、上述したように、制御部90が、第2熱交換器12の出口過冷却度SC2を指標として、絞り装置17の開度OPを制御する。これにより、除湿運転モードにおいて、室内300の温度低下を抑制しながら、室内300の湿度を低下させる除湿運転が可能となる。 In Embodiment 1, as described above, the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC2 of the second heat exchanger 12 as an index. As a result, in the dehumidifying operation mode, it is possible to perform a dehumidifying operation that reduces the humidity in the room 300 while suppressing a temperature drop in the room 300 .

 なお、除湿運転モードにおいて、制御部90が、以下のような制御を実施してもよい。上述したように、給気ファン14の回転数および還気ファン15の回転数は、室内300の必要換気量に応じてあらかじめ決定されるものである。ただし、空気調和装置200のほかに換気装置が設けられているなどの理由で、給気ファン14の回転数および還気ファン15の回転数を変更できる場合がある。その場合は、絞り装置17の開度OPの代わりに、給気ファン14の回転数および還気ファン15の回転数を変更することで、出口過冷却度SC2を制御するようにしてもよい。その場合には、制御部90は、出口過冷却度SC2が閾値Th4以下の場合は、給気ファン14の回転数および還気ファン15の回転数を上昇させることにより、出口過冷却度SC2を増加させる。一方、出口過冷却度SC2が閾値Th4より大きい場合は、制御部90は、給気ファン14の回転数および還気ファン15の回転数を低下させることにより、出口過冷却度SC2を減少させる。なお、この場合に限らず、絞り装置17の開度OPの制御と、給気ファン14の回転数および還気ファン15の回転数の制御とを、併用してもよい。 In addition, in the dehumidifying operation mode, the control unit 90 may perform the following control. As described above, the number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 are determined in advance according to the required ventilation amount of the room 300 . However, there are cases where the number of rotations of the supply air fan 14 and the number of rotations of the return air fan 15 can be changed, for example, because a ventilator is provided in addition to the air conditioner 200 . In that case, the outlet supercooling degree SC2 may be controlled by changing the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 instead of the opening degree OP of the expansion device 17. FIG. In this case, when the outlet supercooling degree SC2 is equal to or less than the threshold value Th4, the control unit 90 increases the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 to reduce the outlet supercooling degree SC2. increase. On the other hand, when the outlet supercooling degree SC2 is greater than the threshold value Th4, the controller 90 decreases the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 to decrease the outlet supercooling degree SC2. Note that the control of the opening degree OP of the expansion device 17 and the control of the rotation speed of the supply air fan 14 and the rotation speed of the return air fan 15 may be used in combination without being limited to this case.

 また、制御部90が、圧縮機16の吸入冷媒圧力と、第3熱交換器13の出口冷媒温度とに基づいて、絞り装置17の開度OPを制御するようにしてもよい。その場合、制御部90は、吸入圧力検出部87の吸入冷媒圧力に基づいて、当該圧力における飽和温度を算出する。次に、制御部90は、算出した飽和温度と、第3冷媒温度検出部85の冷媒温度とに基づいて、第3熱交換器13の出口過熱度SHeを算出する。制御部90は、出口過熱度SHeが閾値Th5以下のとき、圧縮機16への液吸入を防止するために、絞り装置17の開度OPを現在の開度より減少させる。また、制御部90は、出口過熱度SHeが閾値Th5より大きい場合には、絞り装置17の開度OPを現在の値に維持させる。 Also, the control unit 90 may control the opening degree OP of the expansion device 17 based on the refrigerant suction pressure of the compressor 16 and the outlet refrigerant temperature of the third heat exchanger 13 . In that case, the control unit 90 calculates the saturation temperature at the pressure based on the refrigerant suction pressure detected by the suction pressure detection unit 87 . Next, the control unit 90 calculates the outlet superheat degree SHe of the third heat exchanger 13 based on the calculated saturation temperature and the refrigerant temperature of the third refrigerant temperature detection unit 85 . The control unit 90 reduces the opening degree OP of the expansion device 17 from the current opening degree in order to prevent the liquid from being sucked into the compressor 16 when the outlet superheat degree SHe is equal to or less than the threshold value Th5. Further, when the outlet superheat degree SHe is greater than the threshold value Th5, the control unit 90 maintains the opening degree OP of the expansion device 17 at the current value.

 また、制御部90が、圧縮機16の吐出冷媒圧力と、圧縮機16の吐出冷媒温度とに基づいて、絞り装置17の開度OPを制御するようにしてもよい。その場合、制御部90は、吐出圧力検出部86の冷媒圧力に基づいて、当該圧力における飽和温度を算出する。制御部90は、算出した飽和温度と、吐出温度検出部88の冷媒温度とに基づいて、圧縮機16の吐出過熱度SHdを算出する。制御部90は、予め設定された吐出温度の閾値Th6-1と、吐出過熱度SHdの閾値Th6-2に応じて絞り装置17の開度OPを制御する。吐出温度検出部88が閾値Th6-1以上の場合は、絞り装置17の開度OPを増加させる制御を実施する。これにより、蒸発器として機能する第3熱交換器13の出口冷媒を湿り状態にして、圧縮機16に微量の液冷媒を吸入させ、圧縮機16の吐出温度を低下させる。吐出温度検出部88が閾値Th6-1未満の場合は、絞り装置17の開度OPを現在の値に維持する。吐出過熱度SHdが閾値Th6-2以下の場合は、絞り装置17の開度OPを減少させる制御を実施する。これにより、圧縮機16への過剰な液流入を防止することができる。吐出過熱度SHdが閾値Th6-2より大きい場合は、絞り装置17の開度OPを現在の値に維持する。 Also, the control unit 90 may control the opening degree OP of the expansion device 17 based on the pressure of the refrigerant discharged from the compressor 16 and the temperature of the refrigerant discharged from the compressor 16 . In that case, the controller 90 calculates the saturation temperature at the pressure based on the refrigerant pressure detected by the discharge pressure detector 86 . The controller 90 calculates the discharge superheat SHd of the compressor 16 based on the calculated saturation temperature and the refrigerant temperature of the discharge temperature detector 88 . The control unit 90 controls the opening degree OP of the throttle device 17 in accordance with the preset threshold value Th6-1 for the ejection temperature and the threshold value Th6-2 for the ejection superheat degree SHd. When the ejection temperature detection unit 88 is equal to or higher than the threshold value Th6-1, control is performed to increase the opening degree OP of the expansion device 17 . As a result, the refrigerant at the outlet of the third heat exchanger 13 functioning as an evaporator is brought into a wet state, causing the compressor 16 to suck in a small amount of liquid refrigerant, thereby lowering the discharge temperature of the compressor 16 . When the discharge temperature detection unit 88 is less than the threshold value Th6-1, the opening degree OP of the expansion device 17 is maintained at the current value. When the discharge superheat SHd is equal to or less than the threshold value Th6-2, control is performed to decrease the opening degree OP of the expansion device 17 . As a result, excessive inflow of liquid into the compressor 16 can be prevented. When the degree of discharge superheat SHd is greater than the threshold value Th6-2, the opening degree OP of the expansion device 17 is maintained at the current value.

 (運転モードの切替動作)
 次に、冷房運転モードと除湿運転モードとの運転モードの切替動作について説明する。上述した冷房運転モードおよび除湿運転モードは、制御部90が絞り装置17の開度OPを制御するによって、連続的に切り替えることが可能である。図8は、実施の形態1に係る空気調和装置200における絞り装置17の開度OPによる運転モードの切替動作を示す説明図である。図8のグラフにおいて、横軸は、図3および図6の状態R2における冷媒の温度、並びに、絞り装置17の開度OPを示す。なお、横軸において、Tは、外気OAの温度であり、Tは、還気RAの温度である。また、絞り装置17の開度OPの境界点OPは、冷房運転モードおよび除湿運転モードが切り替わる境目である。絞り装置17の開度OPが境界点OPより大きい第2範囲内のとき、除湿運転モードになり、絞り装置17の開度OPが境界点OP以下の第1範囲内のとき、冷房運転モードになる。また、図8のグラフにおいて、縦軸は、第2熱交換器12の冷却能力および加熱能力を示す。縦軸において、0より大きい領域は加熱能力を示し、0以下の領域は、冷却能力を示す。
(Operation mode switching operation)
Next, the switching operation between the cooling operation mode and the dehumidifying operation mode will be described. The cooling operation mode and the dehumidifying operation mode described above can be continuously switched by the control unit 90 controlling the opening degree OP of the expansion device 17 . FIG. 8 is an explanatory diagram showing the operation mode switching operation according to the opening degree OP of the expansion device 17 in the air conditioner 200 according to Embodiment 1. FIG. In the graph of FIG. 8, the horizontal axis indicates the temperature of the refrigerant in the state R2 of FIGS. 3 and 6 and the degree of opening OP of the expansion device 17. On the horizontal axis, T o is the temperature of the outside air OA, and T R is the temperature of the return air RA. A boundary point OP A of the degree of opening OP of the expansion device 17 is a boundary at which the cooling operation mode and the dehumidifying operation mode are switched. When the opening degree OP of the expansion device 17 is within a second range larger than the boundary point OP A , the dehumidifying operation mode is entered, and when the opening degree OP of the expansion device 17 is within a first range below the boundary point OP A , the cooling operation is performed. become a mode. In addition, in the graph of FIG. 8, the vertical axis indicates the cooling capacity and heating capacity of the second heat exchanger 12 . On the vertical axis, the area greater than 0 indicates heating capacity, and the area below 0 indicates cooling capacity.

 図8に示すように、絞り装置17の開度OPが第1範囲内のとき、図3および図6の状態R2の圧力は高くなるため、空気の温度と冷媒の飽和温度との差が大きく、熱交換が促進される。したがって、熱交換後の冷媒の温度は、還気RAの温度Tと同程度となる。このとき、還気RAの温度Tは、外気OAの温度Tよりも低いため、第2熱交換器12は蒸発器として作用する。すなわち、空気調和装置200の運転モードは、冷房運転モードとなる。このとき、絞り装置17の開度OPを境界点OPに向けて大きくしていくと、開度OPが大きくなるにしたがって、状態R2の圧力が低下し、熱交換量が小さくなる。その結果、絞り装置17の開度OPを境界点OPに到達すると、状態R2の冷媒温度は外気OAの温度Tと等しくなる。このとき、第2熱交換器12は熱交換しない。さらに、絞り装置17の開度OPを大きくして第2範囲内の値にすると、状態R2の冷媒温度は、外気OAの温度Tを上回るため、第2熱交換器12は、凝縮器として作用する。すなわち、空気調和装置200の運転モードは、除湿運転モードとなる。 As shown in FIG. 8, when the opening degree OP of the expansion device 17 is within the first range, the pressure in state R2 in FIGS. , heat exchange is facilitated. Therefore, the temperature of the refrigerant after heat exchange becomes approximately the same as the temperature TR of the return air RA. At this time, since the temperature T R of the return air RA is lower than the temperature T O of the outside air OA, the second heat exchanger 12 acts as an evaporator. That is, the operation mode of the air conditioner 200 becomes the cooling operation mode. At this time, if the opening degree OP of the expansion device 17 is increased toward the boundary point OPA , the pressure in the state R2 decreases and the heat exchange amount decreases as the opening degree OP increases. As a result, when the opening degree OP of the expansion device 17 reaches the boundary point OPA, the refrigerant temperature in the state R2 becomes equal to the temperature T O of the outside air OA. At this time, the second heat exchanger 12 does not exchange heat. Furthermore, when the opening degree OP of the expansion device 17 is increased to a value within the second range, the refrigerant temperature in the state R2 exceeds the temperature TO of the outside air OA, so the second heat exchanger 12 functions as a condenser. works. That is, the operation mode of the air conditioner 200 becomes the dehumidification operation mode.

 (運転モードの切替時の制御部90の動作)
 制御部90による運転モードの切替動作について説明する。図9は、実施の形態1に係る空気調和装置200における制御部90の運転モードの切替動作を示すフローチャートである。ステップS21で、制御部90は、還気RAの温度と湿度とを検出する第2温度湿度検出部81から、被空調空間である室内300の温度Troomおよび絶対湿度Xroomを取得する。次に、ステップS22で、制御部90は、被空調空間の温度Troomと閾値Th7とを比較する。温度Troomが閾値Th7よりも高い場合、制御部90は、ステップS23の処理に進み、冷房運転モードの運転を実施する。一方、温度Troomが閾値Th7以下の場合、制御部90は、ステップS24の処理に進む。ステップS24で、制御部90は、被空調空間である室内300の絶対湿度Xroomと閾値Th8とを比較する。絶対湿度Xroomが閾値Th8より高い場合、制御部90は、ステップS25の処理に進み、除湿運転モードの運転を実施する。一方、絶対湿度Xroomが閾値Th8以下の場合、制御部90は、ステップS26の処理に進む。ステップS26では、制御部90は、空気調和装置200において、圧縮機16を停止させることによりヒートポンプ回路は動作させず、還気ファン15および給気ファン14の少なくとも一方を動作させて換気のみを実施する。
(Operation of control unit 90 when switching operation mode)
A switching operation of the operation mode by the control unit 90 will be described. FIG. 9 is a flowchart showing the operation mode switching operation of the control unit 90 in the air conditioner 200 according to Embodiment 1. As shown in FIG. In step S21, the control unit 90 acquires the temperature T room and the absolute humidity X room of the room 300, which is the space to be air-conditioned, from the second temperature/humidity detection unit 81 that detects the temperature and humidity of the return air RA. Next, in step S22, the controller 90 compares the temperature T room of the air-conditioned space with a threshold value Th7. When the temperature T room is higher than the threshold value Th7, the control unit 90 proceeds to the process of step S23 and operates in the cooling operation mode. On the other hand, when the temperature T room is equal to or lower than the threshold value Th7, the control unit 90 proceeds to the process of step S24. In step S24, the controller 90 compares the absolute humidity X room of the room 300, which is the space to be air-conditioned, with the threshold value Th8. When the absolute humidity X room is higher than the threshold value Th8, the control unit 90 proceeds to the process of step S25 and performs operation in the dehumidifying operation mode. On the other hand, when the absolute humidity X room is equal to or lower than the threshold Th8, the control section 90 proceeds to the process of step S26. In step S26, the control unit 90 stops the compressor 16 in the air conditioner 200 so as not to operate the heat pump circuit, and operates at least one of the return air fan 15 and the supply air fan 14 to perform only ventilation. do.

 なお、閾値Th7は、予め設定された固定値であってもよいが、空気調和装置200に対してユーザーから設定される室内300の室温に対する設定値に基づいて決定されてもよい。また、閾値Th8は、予め設定された固定値であってもよいが、空気調和装置200に対してユーザーから設定される室内300の湿度に対する設定値または室温に対する設定値に基づいて決定されてもよい。閾値Th7および閾値Th8の決定方法としては、上記の閾値Th1およびTh4と同様に、データテーブルまたは演算式により求めればよい。 Note that the threshold Th7 may be a preset fixed value, or may be determined based on a set value for the room temperature of the room 300 set by the user for the air conditioner 200 . In addition, the threshold Th8 may be a preset fixed value, or may be determined based on a set value for the humidity of the room 300 or a set value for the room temperature set by the user for the air conditioner 200. good. The threshold Th7 and the threshold Th8 may be determined using a data table or an arithmetic expression in the same manner as the thresholds Th1 and Th4.

 [第1熱交換器11および第2熱交換器12の伝熱管の構成]
 図10は、実施の形態1に係る空気調和装置200における第1熱交換器11および第2熱交換器12の伝熱管の構成を示す側面図である。図10(a)は、第1熱交換器11の伝熱管100の構成の一例を示し、図10(b)は、第2熱交換器12の伝熱管101の構成の一例を示す。
[Configuration of Heat Transfer Tubes of First Heat Exchanger 11 and Second Heat Exchanger 12]
10 is a side view showing the configuration of the heat transfer tubes of the first heat exchanger 11 and the second heat exchanger 12 in the air conditioner 200 according to Embodiment 1. FIG. 10(a) shows an example of the configuration of the heat transfer tubes 100 of the first heat exchanger 11, and FIG. 10(b) shows an example of the configuration of the heat transfer tubes 101 of the second heat exchanger 12. FIG.

 図10(a)に示すように、第1熱交換器11の伝熱管100は、一定間隔を空けて鉛直方向に沿って並んで配置されている。伝熱管100は、円管形状を有している。伝熱管100は、フィン102を貫通するように配置されている。 As shown in FIG. 10(a), the heat transfer tubes 100 of the first heat exchanger 11 are arranged vertically at regular intervals. The heat transfer tube 100 has a circular tubular shape. The heat transfer tubes 100 are arranged to pass through the fins 102 .

 図10(b)に示すように、第2熱交換器12の伝熱管101は、一定間隔を空けて鉛直方向に沿って並んで配置されている。伝熱管101は、フィン103を貫通するように配置されている。伝熱管101は、長径と短径とを有する扁平管形状を有している。伝熱管101の短径は鉛直方向に延びており、伝熱管101の長径は、鉛直方向に対して垂直な方向(すなわち、水平方向)に延びている。伝熱管101を扁平管形状にすることにより、一断面あたりの伝熱管の外周長さを、円管よりも長くすることが可能になる。実施の形態1では、伝熱管101は、伝熱管100よりも、外周長さが長い。その分だけ、伝熱管101は、伝熱管100よりも、伝熱面積が大きくなる。 As shown in FIG. 10(b), the heat transfer tubes 101 of the second heat exchanger 12 are arranged vertically at regular intervals. The heat transfer tubes 101 are arranged to pass through the fins 103 . The heat transfer tube 101 has a flat tube shape having a major axis and a minor axis. The short diameter of heat transfer tube 101 extends in the vertical direction, and the long diameter of heat transfer tube 101 extends in a direction perpendicular to the vertical direction (that is, in the horizontal direction). By forming the heat transfer tube 101 into a flat tube shape, it becomes possible to make the outer circumference length of the heat transfer tube per cross section longer than that of a circular tube. In Embodiment 1, heat transfer tube 101 has a longer outer circumference than heat transfer tube 100 . The heat transfer area of the heat transfer tube 101 is correspondingly larger than that of the heat transfer tube 100 .

 さらに、図10(b)では、伝熱管101が、扁平多孔管から構成されている場合を例示している。伝熱管101の内部は、内柱101aによって区分けされて細管化されることで、直径の小さい複数の冷媒流路101bが形成されている。これに対して、図10(a)に示す円管の伝熱管100では、直径の大きい1つの冷媒流路100bが設けられている。図10(b)の伝熱管101は、細分化されていない扁平管と比較すると、当該細分化により、1断面における冷媒と管内部との接触長さを2倍以上にすることができる。これにより、伝熱管101の管内の伝熱面積を拡大することができる。 Furthermore, FIG. 10(b) illustrates a case where the heat transfer tube 101 is made of a flat perforated tube. The inside of the heat transfer tube 101 is partitioned by the inner column 101a to form a plurality of small-diameter refrigerant flow paths 101b. On the other hand, in the circular heat transfer tube 100 shown in FIG. 10(a), one refrigerant channel 100b having a large diameter is provided. In the heat transfer tube 101 of FIG. 10(b), the contact length between the refrigerant and the inside of the tube in one cross section can be doubled or more due to the subdivision as compared with a flat tube that is not subdivided. Thereby, the heat transfer area inside the heat transfer tube 101 can be increased.

 除湿運転モードにおける第2熱交換器12の加熱能力の最大値は、第1熱交換器11との伝熱面積の比によって大きな影響を受ける。第2熱交換器12の加熱能力と第3熱交換器13の冷却能力とが釣り合った運転状態(除湿のみ)を実現するためには、第1熱交換器11に比べて第2熱交換器12の伝熱面積が大きいほうが望ましい。 The maximum value of the heating capacity of the second heat exchanger 12 in the dehumidifying operation mode is greatly affected by the ratio of the heat transfer area to the first heat exchanger 11. In order to realize an operating state (dehumidification only) in which the heating capacity of the second heat exchanger 12 and the cooling capacity of the third heat exchanger 13 are balanced, the second heat exchanger must be It is desirable that the heat transfer area of 12 is large.

 そこで、実施の形態1では、第2熱交換器12の伝熱管101を扁平管形状にする。これにより、上述したように、一断面あたりの伝熱管101の外周長さを伝熱管100よりも長くすることで、伝熱管101の伝熱面積を、第1熱交換器11の伝熱管100よりも大きくする。また、伝熱管101の内部を細分化することで、さらに、伝熱面積を拡大できる。また、風の進行方向から見たときの伝熱管の投影面積は、扁平管の方が円管より小さくなる。そのため、円管と同じ通風抵抗で設計した場合、伝熱管101を円管に対して高密度に配置することができる。すなわち、図10(a)では、伝熱管100が3本設けられている領域に、図10(b)では、4本の伝熱管101の配置が可能になっている。これにより、伝熱管101とフィン103との接触長さが増加し、フィン103の効率が改善される。また、円管の伝熱管100の場合、フィン102に伝熱管100を挿入してから、伝熱管100を拡管することでフィン102に密着させる。しかしながら、伝熱管100とフィン102との間に、わずかでも空気層が介在すれば熱抵抗となり、性能が低下する。一方、扁平管の伝熱管101の場合は、ロウ付け接続により、フィン103と伝熱管101とを溶着させるため、熱抵抗が小さくなる。これらの理由により、第1熱交換器11に比べて第2熱交換器12の伝熱面積が大きくなり、第2熱交換器12の加熱能力と第3熱交換器13の冷却能力とが釣り合った運転状態(除湿のみ)を実現することが可能になる。なお、第3熱交換器13の伝熱管は、特に限定されず、第2熱交換器12の伝熱管101と同じ扁平管形状であっても、第1熱交換器11の伝熱管100と同じ円管形状であってもよい。 Therefore, in Embodiment 1, the heat transfer tubes 101 of the second heat exchanger 12 are made flat. Thereby, as described above, by making the outer peripheral length of the heat transfer tube 101 per cross section longer than that of the heat transfer tube 100, the heat transfer area of the heat transfer tube 101 is made larger than that of the heat transfer tube 100 of the first heat exchanger 11. also increase. Further, by subdividing the inside of the heat transfer tube 101, the heat transfer area can be further increased. In addition, the projected area of the heat transfer tubes when viewed from the direction of air flow is smaller for the flat tubes than for the circular tubes. Therefore, when designed with the same airflow resistance as that of a circular tube, the heat transfer tubes 101 can be arranged at a high density with respect to the circular tube. That is, in FIG. 10(a), four heat transfer tubes 101 can be arranged in the area where three heat transfer tubes 100 are provided, in FIG. 10(b). This increases the contact length between the heat transfer tubes 101 and the fins 103 and improves the efficiency of the fins 103 . In the case of circular heat transfer tubes 100 , the heat transfer tubes 100 are inserted into the fins 102 and then expanded so that the heat transfer tubes 100 are brought into close contact with the fins 102 . However, if even a small air layer is interposed between the heat transfer tube 100 and the fins 102, it becomes thermal resistance and the performance is lowered. On the other hand, in the case of the flat heat transfer tube 101, the fins 103 and the heat transfer tube 101 are welded together by brazing, so that the thermal resistance is reduced. For these reasons, the heat transfer area of the second heat exchanger 12 is larger than that of the first heat exchanger 11, and the heating capacity of the second heat exchanger 12 and the cooling capacity of the third heat exchanger 13 are balanced. It is possible to achieve a stable operating state (only dehumidification). The heat transfer tubes of the third heat exchanger 13 are not particularly limited, and even if they have the same flat tube shape as the heat transfer tubes 101 of the second heat exchanger 12, It may have a circular tubular shape.

 また、冷房運転モードにおいては第2熱交換器12が液冷媒で満たされ、除湿運転モードにおいては第2熱交換器12が液冷媒または二相冷媒で満たされる。したがって、冷房運転モードと除湿運転モードでは、運転に必要な冷媒充填量が大きく異なる。いずれかの運転モードにとって適正な冷媒充填量とした場合、もう一方の運転モードで安定した運転が困難となる。このような運転モードによる必要冷媒量の変動を抑制するためには、第2熱交換器12の冷媒流路101bの容積を小さくすることが効果的である。具体的には、図10(b)に示すように、伝熱管101が、扁平多孔管のような直径の小さな冷媒流路101bを多数有する構造を有していると良い。扁平多孔管は、このような構造により、大きな伝熱面積と小さな冷媒流路容積とを両立することが可能である。このように、第2熱交換器12が、第1熱交換器11に比べて小さな冷媒流路容積を有することにより、運転モードの違いによる熱交換器内の冷媒量の変動を抑制し、空気調和装置200の動作の安定性を向上させることができる。また、第2熱交換器12で生じた冷媒の過不足を第1熱交換器11で吸収することが可能となる。 Also, in the cooling operation mode, the second heat exchanger 12 is filled with liquid refrigerant, and in the dehumidifying operation mode, the second heat exchanger 12 is filled with liquid refrigerant or two-phase refrigerant. Therefore, the refrigerant charging amount required for operation differs greatly between the cooling operation mode and the dehumidifying operation mode. If the amount of refrigerant charged is appropriate for one of the operation modes, it becomes difficult to achieve stable operation in the other operation mode. Reducing the volume of the refrigerant flow path 101b of the second heat exchanger 12 is effective in suppressing fluctuations in the required amount of refrigerant due to such operation modes. Specifically, as shown in FIG. 10(b), the heat transfer tube 101 preferably has a structure having a large number of small-diameter refrigerant flow paths 101b, such as a flat perforated tube. Due to such a structure, the flat perforated pipe can achieve both a large heat transfer area and a small coolant channel volume. In this way, the second heat exchanger 12 has a smaller refrigerant passage volume than the first heat exchanger 11, thereby suppressing fluctuations in the amount of refrigerant in the heat exchanger due to differences in operation modes, The stability of the operation of the harmony device 200 can be improved. Moreover, it becomes possible for the first heat exchanger 11 to absorb excess or deficiency of the refrigerant generated in the second heat exchanger 12 .

 なお、図10(b)では、第2熱交換器12の伝熱管101が、扁平管形状を有している場合を例に挙げて示している。しかしながら、この場合に限らず、第2熱交換器12が熱交換を行う伝熱面積が、第1熱交換器11が熱交換を行う伝熱面積よりも大きくなる構成であれば、他の構成であってもよい。なお、図10(b)では、第2熱交換器12の伝熱管101が、扁平多孔管から構成されている場合を例に挙げて示している。しかしながら、この場合に限らない。すなわち、第2熱交換器12の伝熱管101が、扁平管形状を有している場合であれば、第2熱交換器12が熱交換を行う伝熱面積が、第1熱交換器11が熱交換を行う伝熱面積よりも大きくなる。そのため、必ずしも、第2熱交換器12の伝熱管101の内部を細分化して多孔管にする必要はない。 Note that FIG. 10(b) shows an example in which the heat transfer tubes 101 of the second heat exchanger 12 have a flat tube shape. However, not limited to this case, as long as the heat transfer area where the second heat exchanger 12 performs heat exchange is larger than the heat transfer area where the first heat exchanger 11 performs heat exchange, other configurations may be In addition, in FIG.10(b), the case where the heat exchanger tube 101 of the 2nd heat exchanger 12 is comprised from a flat perforated tube is mentioned as an example, and is shown. However, it is not limited to this case. That is, if the heat transfer tube 101 of the second heat exchanger 12 has a flat tube shape, the heat transfer area where the second heat exchanger 12 performs heat exchange is Larger than the heat transfer area for heat exchange. Therefore, it is not always necessary to subdivide the inside of the heat transfer tubes 101 of the second heat exchanger 12 into perforated tubes.

 図10(b)では、冷媒流路の容積を小さくするために、第2熱交換器12の伝熱管101が、扁平多孔管から構成されている場合を例に挙げて示している。しかしながら、この場合に限らず、第2熱交換器12の伝熱管101の各冷媒流路101bの容積が、第1熱交換器11の伝熱管100の各冷媒流路の容積よりも小さくなる構成であれば、他の構成であってもよい。 FIG. 10(b) shows an example in which the heat transfer tubes 101 of the second heat exchanger 12 are made of flat perforated tubes in order to reduce the volume of the refrigerant flow path. However, the configuration is not limited to this case, and the volume of each refrigerant flow path 101b of the heat transfer tube 101 of the second heat exchanger 12 is smaller than the volume of each refrigerant flow path of the heat transfer tube 100 of the first heat exchanger 11. If so, other configurations may be used.

 以上のように、実施の形態1では、第2熱交換器12が、第1熱交換器11よりも大きな伝熱面積を有し、第1熱交換器11よりも小さな冷媒流路容積を有している場合について説明した。しかしながら、冷房運転モードを重視して設計する場合にはこの限りではない。 As described above, in Embodiment 1, the second heat exchanger 12 has a larger heat transfer area than the first heat exchanger 11 and a smaller refrigerant flow volume than the first heat exchanger 11. I explained the case where However, this is not the case when designing with a focus on the cooling operation mode.

 [第2熱交換器12および第3熱交換器13の配置]
 第2熱交換器12および第3熱交換器13は、共に、給気経路19内に配置されている。ここでは、給気経路19内における第2熱交換器12および第3熱交換器13の配置について説明する。
[Arrangement of Second Heat Exchanger 12 and Third Heat Exchanger 13]
Both the second heat exchanger 12 and the third heat exchanger 13 are arranged in the air supply path 19 . Here, the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air supply path 19 will be described.

 図11は、実施の形態1に係る空気調和装置200における第2熱交換器12および第3熱交換器13の配置の一例を説明する平面図である。図11では、第2熱交換器12および第3熱交換器13を上から見た状態を示している。また、図11(a)は、実施の形態1における第2熱交換器12および第3熱交換器13の配置例を示し、図11(b)は、比較例を示す。 11 is a plan view illustrating an example of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1. FIG. In FIG. 11, the state which looked at the 2nd heat exchanger 12 and the 3rd heat exchanger 13 from the top is shown. Further, FIG. 11(a) shows an arrangement example of the second heat exchanger 12 and the third heat exchanger 13 in Embodiment 1, and FIG. 11(b) shows a comparative example.

 図11(a)および(b)において、白抜き矢印は、給気経路19内の外気OAの流れる方向を示している。図11(a)に示すように、第2熱交換器12と第3熱交換器13とは、鉛直方向に垂直な方向(すなわち、水平方向)に並んで配置され、且つ、外気OAの流れる方向に対して垂直な方向に並んで配置されている。これにより、給気経路19を流れる外気OAのうち、少なくとも一部分が、第2熱交換器12のみを通過する。これにより、冷房運転モードにおいて、第2熱交換器12が凝縮器として作用することを防ぐことができる。 In FIGS. 11(a) and (b), white arrows indicate the direction in which the outside air OA flows in the air supply path 19. FIG. As shown in FIG. 11( a ), the second heat exchanger 12 and the third heat exchanger 13 are arranged side by side in a direction perpendicular to the vertical direction (that is, in the horizontal direction), and outside air OA flows. They are arranged side by side in a direction perpendicular to the direction. Accordingly, at least part of the outside air OA flowing through the air supply path 19 passes through the second heat exchanger 12 only. This can prevent the second heat exchanger 12 from acting as a condenser in the cooling operation mode.

 従って、実施の形態1においては、少なくとも図11(b)の比較例に示す直列配置は避けることが望ましい。図11(b)では、第2熱交換器12と第3熱交換器13とは、空気の流れる方向に沿って並んで配置されている。すなわち、第2熱交換器12と第3熱交換器13とは、空気の流れる方向において、一方が上流側、他方が下流側に配置されている。例えば図11(b)に示すように、第3熱交換器13が上流側にあると、第3熱交換器13で冷却された空気が第2熱交換器12に流れる。その場合、第2熱交換器12は凝縮器として機能してしまい、冷房運転モードの運転が行えない。逆に、第2熱交換器12が上流側にあると、除湿運転モードにおいて、第2熱交換器12で外気OAを温めた後に、第3熱交換器13で外気OAを冷やす動作となり、除湿量が不十分となる。 Therefore, in Embodiment 1, it is desirable to avoid at least the serial arrangement shown in the comparative example of FIG. 11(b). In FIG. 11(b), the second heat exchanger 12 and the third heat exchanger 13 are arranged side by side along the direction of air flow. That is, one of the second heat exchanger 12 and the third heat exchanger 13 is arranged on the upstream side and the other is arranged on the downstream side in the direction of air flow. For example, as shown in FIG. 11B , if the third heat exchanger 13 is on the upstream side, the air cooled by the third heat exchanger 13 flows to the second heat exchanger 12 . In that case, the second heat exchanger 12 functions as a condenser, and operation in the cooling operation mode cannot be performed. Conversely, if the second heat exchanger 12 is on the upstream side, in the dehumidifying operation mode, after the second heat exchanger 12 warms the outside air OA, the third heat exchanger 13 cools the outside air OA, thereby dehumidifying. Insufficient quantity.

 また、図12は、実施の形態1に係る空気調和装置200における第2熱交換器12および第3熱交換器13の配置の変形例を説明する側面図である。図12では、第2熱交換器12および第3熱交換器13を横から見た状態を示している。図12の変形例のように、第2熱交換器12および第3熱交換器13を鉛直方向に沿って上下に配置するようにしてもよい。具体的には、第2熱交換器12が下側で、第3熱交換器13が上側に配置されている。変形例においても、給気経路19を流れる外気OAのうち、少なくとも一部分が、第2熱交換器12のみを通過する。これにより、冷房運転モードにおいて、第2熱交換器12が凝縮器として作用することを防ぐことができる。 FIG. 12 is a side view explaining a modification of the arrangement of the second heat exchanger 12 and the third heat exchanger 13 in the air conditioner 200 according to Embodiment 1. FIG. FIG. 12 shows a state in which the second heat exchanger 12 and the third heat exchanger 13 are viewed from the side. You may make it arrange|position the 2nd heat exchanger 12 and the 3rd heat exchanger 13 up and down along a perpendicular direction like the modification of FIG. Specifically, the second heat exchanger 12 is arranged on the lower side, and the third heat exchanger 13 is arranged on the upper side. Also in the modified example, at least part of the outside air OA flowing through the air supply path 19 passes only through the second heat exchanger 12 . This can prevent the second heat exchanger 12 from acting as a condenser in the cooling operation mode.

 上記の図5に示すように、空気調和装置200は、冷媒回路上で、1つの絞り装置17と3つの熱交換器11~13を備え、第1熱交換器11は還気経路20内に設置され、第2熱交換器12および第3熱交換器13は給気経路19内に配置されている。除湿運転においては、第2熱交換器12で加熱された空気と、第3熱交換器13で冷却された空気とは、室内300に至るまでに、給気経路19を構成するダクト等で混合され、均一な温度となる。そのため、図12に示すように、第2熱交換器12を第3熱交換器13よりも鉛直方向下側に配置した場合、温度の高い空気は浮力によって上昇するため、当該空気の浮力によって、第2熱交換器12を通過した空気が上昇していく。その結果、第2熱交換器12で加熱された空気と第3熱交換器13で冷却された空気との混合を促進することができる。これにより、室内300にむらの少ない均一な温度の空気を提供し、快適性を向上することが可能となる。 As shown in FIG. 5 above, the air conditioner 200 includes one expansion device 17 and three heat exchangers 11 to 13 on the refrigerant circuit, and the first heat exchanger 11 is in the return air path 20. installed, the second heat exchanger 12 and the third heat exchanger 13 are arranged in the air supply path 19 . In the dehumidification operation, the air heated by the second heat exchanger 12 and the air cooled by the third heat exchanger 13 are mixed in the duct etc. forming the air supply path 19 before reaching the room 300. and a uniform temperature. Therefore, as shown in FIG. 12, when the second heat exchanger 12 is arranged below the third heat exchanger 13 in the vertical direction, high-temperature air rises due to buoyancy. The air that has passed through the second heat exchanger 12 rises. As a result, mixing of the air heated by the second heat exchanger 12 and the air cooled by the third heat exchanger 13 can be promoted. As a result, it is possible to provide air having a uniform temperature with little unevenness in the room 300 and improve comfort.

 以上のように、実施の形態1に係る空気調和装置200では、冷房運転モードと除湿運転モードとにおいて、冷媒回路において冷媒の流れる方向が同じである。冷房運転モードにおいては、絞り装置17の開度OPは第1範囲内に設定されて、第1熱交換器11は凝縮器として作用し、第2熱交換器12および第3熱交換器13が蒸発器として作用する。除湿運転モードにおいては、絞り装置17の開度OPは第1範囲よりも大きい第2範囲内に設定されて、第1熱交換器11および第2熱交換器12は凝縮器として作用し、第3熱交換器13が蒸発器として作用する。このように、実施の形態1に係る空気調和装置200では、流路の切替を必要としない簡易な構成で、除湿運転モードと冷房運転モードとを連続的に移行することができる。そのため、上記の特許文献1とは異なり、流路切り替えに伴う熱交換器内の冷媒圧力の変動を抑制することができる。その結果、実施の形態1では、空気調和装置200によって室内300に給気される給気SAの温度の変動が抑制できるので、安定した温度の給気SAが室内300に供給され、室内300内のユーザーの快適性を向上させることができる。 As described above, in the air conditioner 200 according to Embodiment 1, the refrigerant flows in the same direction in the refrigerant circuit in the cooling operation mode and the dehumidifying operation mode. In the cooling operation mode, the opening degree OP of the expansion device 17 is set within the first range, the first heat exchanger 11 acts as a condenser, and the second heat exchanger 12 and the third heat exchanger 13 are Acts as an evaporator. In the dehumidifying operation mode, the opening degree OP of the expansion device 17 is set within a second range larger than the first range, the first heat exchanger 11 and the second heat exchanger 12 act as condensers, 3 Heat exchanger 13 acts as an evaporator. As described above, the air conditioner 200 according to Embodiment 1 can continuously switch between the dehumidifying operation mode and the cooling operation mode with a simple configuration that does not require switching of the flow path. Therefore, unlike Patent Document 1 described above, it is possible to suppress fluctuations in the pressure of the refrigerant in the heat exchanger that accompany switching of the flow path. As a result, in Embodiment 1, since the temperature fluctuation of the supply air SA supplied to the room 300 by the air conditioner 200 can be suppressed, the supply air SA having a stable temperature is supplied to the room 300, and the temperature inside the room 300 is reduced. of user comfort can be improved.

 また、実施の形態1では、制御部90が、除湿運転モードにおいて、圧縮機16の吐出側または吸入側の冷媒の圧力、第2熱交換器12の出口側の冷媒温度、第3熱交換器13の出口側の冷媒温度、圧縮機16の吐出側の冷媒温度のうちの少なくとも1つに基づいて、絞り装置17の開度OPを制御する。具体的には、制御部90は、絞り装置17の開度OPを第2範囲内で現在の値より減少させることにより、給気ファン14によって給気される室外の空気に対する第2熱交換器12の加熱能力を減少させる。逆に、制御部90は、絞り装置17の開度を第2範囲内で現在の値より増加させることにより、給気ファン14によって給気される室外の空気に対する第2熱交換器12の加熱能力を増加させる。これにより、第2熱交換器12から室内300に供給される空気の温度を制御できるため、室内300の温度低下を抑制しながら、室内300の湿度を低下させる除湿運転が可能となる。 Further, in the first embodiment, in the dehumidification operation mode, the control unit 90 controls the pressure of the refrigerant on the discharge side or the suction side of the compressor 16, the refrigerant temperature on the outlet side of the second heat exchanger 12, the temperature of the refrigerant on the outlet side of the second heat exchanger 12, the The opening degree OP of the throttle device 17 is controlled based on at least one of the refrigerant temperature on the outlet side of the compressor 13 and the refrigerant temperature on the discharge side of the compressor 16 . Specifically, the control unit 90 reduces the opening degree OP of the expansion device 17 from the current value within the second range so that the second heat exchanger for the outdoor air supplied by the air supply fan 14 Decrease the heating capacity of 12. Conversely, the control unit 90 increases the degree of opening of the expansion device 17 within the second range from the current value so that the outdoor air supplied by the supply fan 14 is heated by the second heat exchanger 12 . increase capacity. As a result, the temperature of the air supplied from the second heat exchanger 12 to the room 300 can be controlled, so that the dehumidification operation that reduces the humidity in the room 300 can be performed while suppressing the temperature drop in the room 300 .

 実施の形態2.
 実施の形態2に係る空気調和装置200Bについて説明する。図13は、実施の形態2に係る空気調和装置200Bの構成の一例を示す冷媒回路図である。実施の形態1で説明した図1の構成と比較すると、図13においては、第1開閉弁21、第2開閉弁22、および、バイパス配管23が追加されている点が異なる。他の構成については、図1と同じであるため、同一符号を付して示し、ここでは、その説明を省略する。
Embodiment 2.
An air conditioner 200B according to Embodiment 2 will be described. FIG. 13 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200B according to Embodiment 2. As shown in FIG. Compared with the configuration of FIG. 1 described in Embodiment 1, the configuration of FIG. Since other configurations are the same as those in FIG. 1, they are denoted by the same reference numerals, and descriptions thereof are omitted here.

 第1開閉弁21は、第1熱交換器11と第2熱交換器12との間の冷媒配管18に設けられている。第1開閉弁21の開閉動作は、制御部90によって制御される。 The first on-off valve 21 is provided in the refrigerant pipe 18 between the first heat exchanger 11 and the second heat exchanger 12 . The opening/closing operation of the first opening/closing valve 21 is controlled by the controller 90 .

 バイパス配管23は、冷媒配管18から分岐したバイパス配管である。バイパス配管23は、第1熱交換器11と第1開閉弁21との間の点C1において冷媒配管18から分岐している。また、バイパス配管23は、第2熱交換器12と絞り装置17との間の点C2において冷媒配管18に接続している。このとき、第2冷媒温度検出部84は、バイパス配管23よりも下流側に配置されている。 A bypass pipe 23 is a bypass pipe branched from the refrigerant pipe 18 . The bypass pipe 23 branches off from the refrigerant pipe 18 at a point C<b>1 between the first heat exchanger 11 and the first on-off valve 21 . Also, the bypass pipe 23 is connected to the refrigerant pipe 18 at a point C2 between the second heat exchanger 12 and the expansion device 17 . At this time, the second refrigerant temperature detector 84 is arranged downstream of the bypass pipe 23 .

 第2開閉弁22は、バイパス配管23に設けられている。第2開閉弁22が開状態のとき、バイパス配管23に冷媒が流れる。第2開閉弁22の開閉動作は、制御部90によって制御される。 The second on-off valve 22 is provided on the bypass pipe 23 . When the second on-off valve 22 is open, refrigerant flows through the bypass pipe 23 . The opening/closing operation of the second opening/closing valve 22 is controlled by the controller 90 .

 次に、実施の形態2に係る空気調和装置200Bの動作について説明する。実施の形態2においては、除湿運転モードにおいては、制御部90が、第1開閉弁21を開き、第2開閉弁22を閉じる。これにより、実施の形態2の除湿運転モードの動作は、実施の形態1の除湿運転モードの動作と同じになる。 Next, the operation of the air conditioner 200B according to Embodiment 2 will be described. In Embodiment 2, the controller 90 opens the first on-off valve 21 and closes the second on-off valve 22 in the dehumidifying operation mode. As a result, the operation in the dehumidifying operation mode of the second embodiment is the same as the operation in the dehumidifying operation mode of the first embodiment.

 冷房運転モードでは、制御部90は、外気OAの温度Tが還気RAの温度Tより大きく、且つ、外気OAの温度Tと還気RAの温度Tとの温度差ΔTが閾値Th9より大きい場合は、第1開閉弁21を開き、第2開閉弁22を閉じる。この場合の実施の形態2の冷房運転モードの動作は、実施の形態1の冷房運転モードの動作と同じになる。 In the cooling operation mode, the controller 90 sets the temperature T 0 of the outside air OA to be higher than the temperature T R of the return air RA, and the temperature difference ΔT between the temperature T 0 of the outside air OA and the temperature T R of the return air RA. If it is greater than Th9, the first on-off valve 21 is opened and the second on-off valve 22 is closed. The operation in the cooling operation mode of the second embodiment in this case is the same as the operation in the cooling operation mode of the first embodiment.

 なお、閾値Th9は、通常の冷房運転を想定した外気OAの温度Tと還気RAの温度Tとの温度差ΔTの設計値(すなわち、通常運転時の理論値)に基づいて予め設定した固定値であってもよいが、可変の値でもよい。その場合、例えば、閾値Th9は、制御部90によって、空気調和装置200に対してユーザーから設定される室内300の室温に対する設定値、あるいは、外気OAの温度Tと還気RAの温度Tとの温度差に基づいて決定される。なお、決定方法としては、データテーブルまたは演算式をメモリに予め格納しておき、制御部90が、それを用いて閾値Th9を演算する。当該データテーブルには、室温に対する設定値あるいは温度差ごとに、閾値Th9を記憶しておく。また、演算式は、室温に対する設定値あるいは温度差をパラメータとして閾値Th9を求める関数である。 The threshold Th9 is set in advance based on the design value of the temperature difference ΔT between the temperature T O of the outside air OA and the temperature T R of the return air RA assuming normal cooling operation (that is, the theoretical value during normal operation). It may be a fixed value, or a variable value. In that case, for example, the threshold value Th9 is a set value for the room temperature of the room 300 set by the user for the air conditioner 200 by the control unit 90, or the temperature T O of the outside air OA and the temperature T R of the return air RA. is determined based on the temperature difference between As a determination method, a data table or an arithmetic expression is stored in advance in the memory, and the control unit 90 uses it to calculate the threshold value Th9. The data table stores a threshold value Th9 for each set value or temperature difference with respect to the room temperature. The arithmetic expression is a function for obtaining the threshold value Th9 using the set value or the temperature difference with respect to the room temperature as a parameter.

 一方、冷房運転モードにおいて、外気OAの温度Tと還気RAの温度Tとの温度差ΔTが閾値Th9以下の場合、あるいは、外気OAの温度Tが還気RAの温度T以下の場合は、制御部90は、第1開閉弁21を閉じ、第2開閉弁22を開く。これにより、冷媒はバイパス配管23を流れるようになり、バイパス配管23から絞り装置17を介して第3熱交換器13に流入される。すなわち、冷媒は、第2熱交換器12をスキップして、第1熱交換器11、バイパス配管23、絞り装置17、第3熱交換器13の順に流れる。これにより、外気OAと還気RAの温度差ΔTが小さい場合、冷房運転モードで、本来は蒸発器として作動する第2熱交換器12が、凝縮器として作動することを防ぐことができる。 On the other hand, in the cooling operation mode, when the temperature difference ΔT between the temperature T O of the outside air OA and the temperature T R of the return air RA is equal to or less than the threshold value Th9, or the temperature T O of the outside air OA is equal to or less than the temperature T R of the return air RA. , the controller 90 closes the first on-off valve 21 and opens the second on-off valve 22 . As a result, the refrigerant flows through the bypass pipe 23 and flows from the bypass pipe 23 through the expansion device 17 into the third heat exchanger 13 . That is, the refrigerant skips the second heat exchanger 12 and flows through the first heat exchanger 11, the bypass pipe 23, the expansion device 17, and the third heat exchanger 13 in this order. As a result, when the temperature difference ΔT between the outside air OA and the return air RA is small, the second heat exchanger 12, which originally operates as an evaporator, can be prevented from operating as a condenser in the cooling operation mode.

 (制御部90)
 図14は、実施の形態2に係る空気調和装置200Bにおける制御部90の動作を示すフローチャートである。ステップS31で、制御部90は、空気調和装置200Bの現在の運転モードが、除湿運転モードか冷房運転モードかを判定する。制御部90は、空気調和装置200Bの現在の運転モードが除湿運転モードである場合は、ステップS32の処理に進む。一方、制御部90は、空気調和装置200Bの現在の運転モードが冷房運転モードである場合は、ステップS33の処理に進む。
(control unit 90)
FIG. 14 is a flow chart showing the operation of the control unit 90 in the air conditioner 200B according to Embodiment 2. As shown in FIG. In step S31, the controller 90 determines whether the current operation mode of the air conditioner 200B is the dehumidifying operation mode or the cooling operation mode. If the current operation mode of the air conditioner 200B is the dehumidifying operation mode, the control unit 90 proceeds to the process of step S32. On the other hand, when the current operation mode of the air conditioner 200B is the cooling operation mode, the control unit 90 proceeds to the process of step S33.

 ステップS32では、制御部90は、第1開閉弁21を開き、第2開閉弁22を閉じる。すなわち、実施の形態2の除湿運転モードの動作は、実施の形態1の除湿運転モードの動作と同じになる。 At step S32, the control unit 90 opens the first on-off valve 21 and closes the second on-off valve 22. That is, the operation in the dehumidifying operation mode of the second embodiment is the same as the operation in the dehumidifying operation mode of the first embodiment.

 ステップS33では、制御部90は、外気OAの温度Tが還気RAの温度Tより大きく、且つ、外気OAの温度Tと還気RAの温度Tとの温度差ΔTが閾値Th9より大きいかを判定する。これらの条件をすべて満たしている場合には、制御部90は、ステップS34の処理に進む。そうでない場合には、制御部90は、ステップS35の処理に進む。 In step S33, the controller 90 determines that the temperature T O of the outside air OA is higher than the temperature T R of the return air RA, and that the temperature difference ΔT between the temperature T O of the outside air OA and the temperature T R of the return air RA is a threshold value Th9. Determine if greater than. If all of these conditions are satisfied, the control section 90 proceeds to the process of step S34. Otherwise, the control section 90 proceeds to the process of step S35.

 ステップS34では、制御部90は、第1開閉弁21を開き、第2開閉弁22を閉じる。この場合の実施の形態2の冷房運転モードの動作は、実施の形態1の冷房運転モードの動作と同じになる。 In step S34, the control unit 90 opens the first on-off valve 21 and closes the second on-off valve 22. The operation in the cooling operation mode of the second embodiment in this case is the same as the operation in the cooling operation mode of the first embodiment.

 一方、ステップS35では、制御部90は、第2熱交換器12を蒸発器として作動させることが困難であると判断し、第1開閉弁21を閉じ、第2開閉弁22を開く。 On the other hand, in step S35, the controller 90 determines that it is difficult to operate the second heat exchanger 12 as an evaporator, closes the first on-off valve 21, and opens the second on-off valve 22.

 以上のように、実施の形態2では、基本的に実施の形態1と同じ構成を有しているため、実施の形態1と同様の効果が得られる。さらに、実施の形態2においては、図13に示すように、図1の構成に対して、第1開閉弁21、第2開閉弁22、および、バイパス配管23を追加している。実施の形態2においては、冷房運転モードにおいて、外気OAの温度Tと還気RAの温度Tとの温度差ΔTが小さい場合、あるいは、外気OAの温度Tが還気RAの温度T以下の場合は、制御部90が、第1開閉弁21を閉じ、第2開閉弁22を開く制御を行う。これにより、冷房運転モードにおいて、本来は蒸発器として作動する第2熱交換器12が、凝縮器として作動することを防ぐことができる。 As described above, since the second embodiment basically has the same configuration as the first embodiment, the same effects as those of the first embodiment can be obtained. Furthermore, in Embodiment 2, as shown in FIG. 13, a first on-off valve 21, a second on-off valve 22, and a bypass pipe 23 are added to the configuration of FIG. In the second embodiment, in the cooling operation mode, when the temperature difference ΔT between the temperature T 0 of the outside air OA and the temperature T R of the return air RA is small, or the temperature T 0 of the outside air OA is equal to the temperature T of the return air RA. In the case of R or less, the control unit 90 closes the first on-off valve 21 and performs control to open the second on-off valve 22 . As a result, in the cooling operation mode, the second heat exchanger 12, which originally operates as an evaporator, can be prevented from operating as a condenser.

 実施の形態3.
 実施の形態3に係る空気調和装置200Cについて説明する。図15は、実施の形態3に係る空気調和装置200Cの構成の一例を示す冷媒回路図である。実施の形態1で説明した図1の構成と比較すると、図15においては、第3熱交換器13と圧縮機16との間の冷媒配管18にアキュムレータ24が追加されている点で異なる。アキュムレータ24は、冷媒配管18内の余剰冷媒を貯留する。他の構成については、図1と同じであるため、同一符号を付して示し、ここでは、その説明を省略する。なお、図15では、検出部80~88の図示が省略されているが、実際には、設けられているものとする。
Embodiment 3.
An air conditioner 200C according to Embodiment 3 will be described. FIG. 15 is a refrigerant circuit diagram showing an example of the configuration of an air conditioner 200C according to Embodiment 3. As shown in FIG. 1 described in Embodiment 1 differs in that an accumulator 24 is added to the refrigerant pipe 18 between the third heat exchanger 13 and the compressor 16 in FIG. The accumulator 24 stores excess refrigerant in the refrigerant pipe 18 . Since other configurations are the same as those in FIG. 1, they are denoted by the same reference numerals, and descriptions thereof are omitted here. Although the detection units 80 to 88 are omitted in FIG. 15, they are actually provided.

 実施の形態3においては、除湿運転モードでは、アキュムレータ24に冷媒を貯留することにより、冷媒配管18を循環する冷媒を減らす。 In the third embodiment, in the dehumidifying operation mode, the amount of refrigerant circulating in the refrigerant pipe 18 is reduced by storing the refrigerant in the accumulator 24 .

 一方、冷房運転モードでは、アキュムレータ24に貯留された冷媒を冷媒配管18に放出することにより、冷媒配管18を循環する冷媒を増やす。 On the other hand, in the cooling operation mode, by releasing the refrigerant stored in the accumulator 24 to the refrigerant pipe 18, the refrigerant circulating in the refrigerant pipe 18 is increased.

 これによって、運転モードに応じて、実質的な冷媒充填量を調整する効果を得ることができる。冷媒充填量は、必要冷媒量の最も多い運転モードに合わせると良い。 As a result, it is possible to obtain the effect of adjusting the substantial refrigerant charging amount according to the operation mode. The amount of refrigerant to be charged should be adjusted to the operation mode that requires the largest amount of refrigerant.

 アキュムレータ24への冷媒の貯留と放出は、必要に応じて成り行きで行われる。例えば、制御部90が、第1熱交換器11または第2熱交換器12の出口における冷媒の出口過冷却度SC1またはSC2を指標として、絞り装置17の開度OPを制御する場合について考える。冷房運転モードにおいて、第1熱交換器11の出口過冷却度SC1を増加させるとき、絞り装置17を絞ることによって、第3熱交換器13の圧力が下がり、熱交換が促進されることにより、アキュムレータ24に過熱ガスが流入する。したがって、過熱ガスで温められたアキュムレータ24内の液冷媒が冷媒配管18に放出される。一方、除湿運転モードにおいて、第2熱交換器12の出口過冷却度SC2を減少させるとき、絞り装置17を開くことによって、第3熱交換器13の圧力が上がり、熱交換が抑制されることにより、アキュムレータ24に液冷媒が流入する。したがって、アキュムレータ24内に液冷媒が貯留される。  Refrigerant is stored in and discharged from the accumulator 24 as needed. For example, consider a case where the control unit 90 controls the opening degree OP of the expansion device 17 using the outlet subcooling degree SC1 or SC2 of the refrigerant at the outlet of the first heat exchanger 11 or the second heat exchanger 12 as an index. In the cooling operation mode, when increasing the degree of subcooling SC1 at the outlet of the first heat exchanger 11, by throttling the throttling device 17, the pressure of the third heat exchanger 13 is reduced and heat exchange is promoted. Superheated gas flows into the accumulator 24 . Therefore, the liquid refrigerant in the accumulator 24 warmed by the superheated gas is released to the refrigerant pipe 18 . On the other hand, in the dehumidifying operation mode, when the outlet supercooling degree SC2 of the second heat exchanger 12 is decreased, opening the expansion device 17 increases the pressure of the third heat exchanger 13, suppressing heat exchange. As a result, liquid refrigerant flows into the accumulator 24 . Therefore, liquid refrigerant is stored in the accumulator 24 .

 以上のように、実施の形態3では、基本的に実施の形態1と同じ構成を有しているため、実施の形態1と同様の効果が得られる。さらに、実施の形態3では、第3熱交換器13と圧縮機16との間にアキュムレータ24を設けている。これにより、除湿運転モードでは、アキュムレータ24に冷媒を貯留し、冷房運転モードでは、アキュムレータ24に貯留された冷媒を冷媒配管18に放出することにより、冷媒の不足を防止することができる。 As described above, since the third embodiment basically has the same configuration as the first embodiment, the same effect as the first embodiment can be obtained. Furthermore, in Embodiment 3, an accumulator 24 is provided between the third heat exchanger 13 and the compressor 16 . As a result, the refrigerant is stored in the accumulator 24 in the dehumidifying operation mode, and the refrigerant stored in the accumulator 24 is released to the refrigerant pipe 18 in the cooling operation mode, thereby preventing a shortage of refrigerant.

 11 第1熱交換器、12 第2熱交換器、13 第3熱交換器、14 給気ファン、15 還気ファン、16 圧縮機、17 絞り装置、18 冷媒配管、19 給気経路、20 還気経路、21 第1開閉弁、22 第2開閉弁、23 バイパス配管、24 アキュムレータ、30 流路切替装置、31 第2絞り装置、40 飽和蒸気線、41 飽和液線、80 第1温度湿度検出部、81 第2温度湿度検出部、82 外気温度検出部、83 第1冷媒温度検出部、84 第2冷媒温度検出部、85 第3冷媒温度検出部、86 吐出圧力検出部、87 吸入圧力検出部、88 吐出温度検出部、89 第4冷媒温度検出部、90 制御部、100 伝熱管、100b 冷媒流路、101 伝熱管、101a 内柱、101b 冷媒流路、102 フィン、103 フィン、200 空気調和装置、200A 空気調和装置、200B 空気調和装置、200C 空気調和装置、300 室内、301 室外、EA 排気、OA 外気、RA 還気、SA 給気、SC1 第1熱交換器11の出口過冷却度、SC2 第2熱交換器12の出口過冷却度、SHd 圧縮機16の吐出過熱度、SHe 第3熱交換器13の出口過熱度、Th1 閾値、Th2 閾値、Th3-1 閾値、Th3-2 閾値、Th4 閾値(第1閾値)、Th5 閾値、Th6-1 閾値、Th6-2 閾値、Th7 閾値、Th8 閾値、Th9 閾値(第2閾値)。 11 1st heat exchanger, 12 2nd heat exchanger, 13 3rd heat exchanger, 14 supply air fan, 15 return air fan, 16 compressor, 17 expansion device, 18 refrigerant pipe, 19 air supply route, 20 return air path, 21 first on-off valve, 22 second on-off valve, 23 bypass pipe, 24 accumulator, 30 flow path switching device, 31 second expansion device, 40 saturated steam line, 41 saturated liquid line, 80 first temperature and humidity detection Section 81 Second temperature/humidity detection section 82 Outside air temperature detection section 83 First refrigerant temperature detection section 84 Second refrigerant temperature detection section 85 Third refrigerant temperature detection section 86 Discharge pressure detection section 87 Suction pressure detection part, 88 discharge temperature detection part, 89 fourth refrigerant temperature detection part, 90 control part, 100 heat transfer tube, 100b refrigerant flow path, 101 heat transfer tube, 101a inner column, 101b refrigerant flow path, 102 fins, 103 fins, 200 air Conditioner, 200A: Air conditioner, 200B: Air conditioner, 200C: Air conditioner, 300: Indoor, 301: Outdoor, EA: Exhaust, OA: Outside air, RA: Return air, SA: Supply air, SC1: Outlet supercooling degree of first heat exchanger 11 , SC2 Degree of subcooling at the outlet of the second heat exchanger 12, SHd Degree of superheat at the outlet of the compressor 16, SHe Degree of superheat at the outlet of the third heat exchanger 13, Th1 Threshold, Th2 Threshold, Th3-1 Threshold, Th3-2 Threshold , Th4 threshold (first threshold), Th5 threshold, Th6-1 threshold, Th6-2 threshold, Th7 threshold, Th8 threshold, Th9 threshold (second threshold).

Claims (10)

 室外の空気を室内に給気する給気ファンおよび給気経路と、
 前記室内の空気を前記室外に還気する還気ファンおよび還気経路と、
 圧縮機、第1熱交換器、第2熱交換器、絞り装置、第3熱交換器の順に冷媒配管によってこれらが接続されたヒートポンプ回路と、
 前記給気ファン、前記還気ファン、および、前記ヒートポンプ回路の動作の制御を行う制御部と
 を備えた空気調和装置であって、
 前記第1熱交換器は、前記還気経路内に配置され、前記第1熱交換器の内部を流れる冷媒と前記還気経路内を流れる空気との間で熱交換を行い、
 前記第2熱交換器および前記第3熱交換器は、前記給気経路内に配置され、それぞれ、前記第2熱交換器および前記第3熱交換器の内部を流れる冷媒と前記給気経路内を流れる空気との間で熱交換を行い、
 前記空気調和装置は、運転モードとして、前記室内を冷房する冷房運転モードと前記室内を除湿する除湿運転モードとを有し、
 前記除湿運転モードおよび前記冷房運転モードにおいて、前記圧縮機から吐出された冷媒が前記第1熱交換器に流入されて、前記第3熱交換器から流出した冷媒が前記圧縮機に吸入される方向に、前記冷媒配管を冷媒が流れ、
 前記冷房運転モードにおいて、前記第1熱交換器は凝縮器として作用し、前記第2熱交換器および前記第3熱交換器が蒸発器として作用し、
 前記除湿運転モードにおいて、前記第1熱交換器および前記第2熱交換器は凝縮器として作用し、前記第3熱交換器が蒸発器として作用する、
 空気調和装置。
an air supply fan and an air supply path for supplying outdoor air into the room;
a return air fan and a return air path for returning the indoor air to the outdoor;
a heat pump circuit in which a compressor, a first heat exchanger, a second heat exchanger, an expansion device, and a third heat exchanger are connected in this order by refrigerant pipes;
An air conditioner comprising: a control unit that controls operations of the supply air fan, the return air fan, and the heat pump circuit,
The first heat exchanger is arranged in the return air path, and performs heat exchange between the refrigerant flowing inside the first heat exchanger and the air flowing in the return air path,
The second heat exchanger and the third heat exchanger are arranged in the air supply path, and the refrigerant flowing inside the second heat exchanger and the third heat exchanger and the air supply path, respectively heat exchange with the air flowing through the
The air conditioner has, as operation modes, a cooling operation mode for cooling the room and a dehumidifying operation mode for dehumidifying the room,
In the dehumidifying operation mode and the cooling operation mode, the direction in which the refrigerant discharged from the compressor flows into the first heat exchanger and the refrigerant discharged from the third heat exchanger is sucked into the compressor. , the refrigerant flows through the refrigerant pipe,
In the cooling operation mode, the first heat exchanger acts as a condenser, the second heat exchanger and the third heat exchanger act as evaporators,
In the dehumidification mode of operation, the first heat exchanger and the second heat exchanger act as condensers, and the third heat exchanger acts as an evaporator.
Air conditioner.
 前記冷房運転モードにおいて、前記絞り装置の開度は第1範囲内の値に設定され、
 前記除湿運転モードにおいて、前記絞り装置の開度は前記第1範囲よりも大きい第2範囲内の値に設定される、
 請求項1に記載の空気調和装置。
In the cooling operation mode, the degree of opening of the expansion device is set to a value within a first range,
In the dehumidifying operation mode, the opening degree of the expansion device is set to a value within a second range that is larger than the first range.
The air conditioner according to claim 1.
 前記制御部は、前記除湿運転モードにおいて、
 前記絞り装置の開度を前記第2範囲内で現在の値より減少させることにより、前記給気ファンによって給気される前記室外の空気に対する前記第2熱交換器の加熱能力を減少させ、
 前記絞り装置の開度を前記第2範囲内で現在の値より増加させることにより、前記給気ファンによって給気される前記室外の空気に対する前記第2熱交換器の加熱能力を増加させることにより、
 前記第2熱交換器から前記室内に供給される空気の温度を制御する、
 請求項2に記載の空気調和装置。
The control unit, in the dehumidifying operation mode,
reducing the opening degree of the expansion device from the current value within the second range to reduce the heating capacity of the second heat exchanger for the outdoor air supplied by the air supply fan;
By increasing the opening degree of the expansion device from the current value within the second range, thereby increasing the heating capacity of the second heat exchanger for the outdoor air supplied by the air supply fan. ,
controlling the temperature of the air supplied from the second heat exchanger into the room;
The air conditioner according to claim 2.
 前記圧縮機の吐出側の圧力を検出する吐出圧力検出部と、
 前記第2熱交換器の出口側の冷媒温度を検出する冷媒温度検出部と
 を備え、
 前記制御部は、前記除湿運転モードにおいて、
 前記圧縮機の前記吐出側の圧力と前記第2熱交換器の前記出口側の冷媒温度とに基づいて、前記第2熱交換器の出口過冷却度を算出し、
 前記第2熱交換器の前記出口過冷却度が第1閾値以下の場合、前記絞り装置の開度を前記第2範囲内で現在の値より減少させることにより、前記給気ファンによって給気される前記室外の空気に対する前記第2熱交換器の加熱能力を減少させ、
 前記第2熱交換器の前記出口過冷却度が前記第1閾値より大きい場合、前記絞り装置の開度を前記第2範囲内で現在の値より増加させることにより、前記給気ファンによって給気される前記室外の空気に対する前記第2熱交換器の加熱能力を増加させる、
 請求項2または3に記載の空気調和装置。
a discharge pressure detection unit that detects the pressure on the discharge side of the compressor;
A refrigerant temperature detection unit that detects the refrigerant temperature on the outlet side of the second heat exchanger,
The control unit, in the dehumidifying operation mode,
calculating the degree of subcooling at the outlet of the second heat exchanger based on the pressure on the discharge side of the compressor and the refrigerant temperature on the outlet side of the second heat exchanger;
When the degree of supercooling at the outlet of the second heat exchanger is equal to or less than the first threshold, the opening of the expansion device is reduced from the current value within the second range to reduce the amount of air supplied by the supply fan. reducing the heating capacity of the second heat exchanger for the outdoor air,
If the outlet subcooling degree of the second heat exchanger is greater than the first threshold, the opening of the throttling device is increased from the current value within the second range so that air is supplied by the supply fan. increasing the heating capacity of the second heat exchanger for the outdoor air to be
The air conditioner according to claim 2 or 3.
 前記第2熱交換器の前記熱交換を行う伝熱面積は、前記第1熱交換器の前記熱交換を行う伝熱面積より大きい、
 請求項1~4のいずれか1項に記載の空気調和装置。
The heat transfer area for performing the heat exchange of the second heat exchanger is larger than the heat transfer area for performing the heat exchange of the first heat exchanger,
The air conditioner according to any one of claims 1 to 4.
 前記第1熱交換器は、前記冷媒の流れる伝熱管を内部に有し、
 前記第2熱交換器は、前記冷媒の流れる伝熱管を内部に有し、
 前記第2熱交換器の前記伝熱管の前記冷媒が流れる各冷媒流路の容積は、前記第1熱交換器の前記伝熱管の前記冷媒が流れる各冷媒流路の容積より小さい、
 請求項1~5のいずれか1項に記載の空気調和装置。
The first heat exchanger has therein a heat transfer tube through which the refrigerant flows,
The second heat exchanger has therein a heat transfer tube through which the refrigerant flows,
The volume of each refrigerant channel through which the refrigerant flows in the heat transfer tube of the second heat exchanger is smaller than the volume of each refrigerant channel through which the refrigerant flows in the heat transfer tube of the first heat exchanger,
The air conditioner according to any one of claims 1 to 5.
 前記第1熱交換器と前記第2熱交換器との間に配置された第1開閉弁と、
 前記第1熱交換器と前記第1開閉弁との間から分岐して、前記第2熱交換器と前記絞り装置との間に接続されたバイパス配管と、
 前記バイパス配管に設けられた第2開閉弁と
 を備え、
 前記制御部は、
 前記除湿運転モードにおいて、前記第1開閉弁を開き、前記第2開閉弁を閉じ、
 前記冷房運転モードにおいて、
 前記給気ファンによって給気される前記室外の空気の温度と前記還気ファンによって還気される前記室内の空気の温度との温度差が第2閾値より大きい場合は、前記第1開閉弁を開き、前記第2開閉弁を閉じ、
 前記温度差が前記第2閾値以下の場合は、前記第1開閉弁を閉じ、前記第2開閉弁を開く、
 請求項1~6のいずれか1項に記載の空気調和装置。
a first on-off valve arranged between the first heat exchanger and the second heat exchanger;
a bypass pipe branched from between the first heat exchanger and the first on-off valve and connected between the second heat exchanger and the expansion device;
A second on-off valve provided in the bypass pipe,
The control unit
In the dehumidifying operation mode, the first on-off valve is opened, the second on-off valve is closed,
In the cooling operation mode,
When the temperature difference between the temperature of the outdoor air supplied by the supply air fan and the temperature of the indoor air returned by the return air fan is greater than a second threshold, the first on-off valve is closed. open, close the second on-off valve,
when the temperature difference is equal to or less than the second threshold, the first on-off valve is closed and the second on-off valve is opened;
The air conditioner according to any one of claims 1 to 6.
 前記第3熱交換器および前記第2熱交換器は、前記給気経路を流れる空気のうち少なくとも一部分が前記第2熱交換器のみを通過するように前記給気経路内に配置される、
 請求項1~7のいずれか1項に記載の空気調和装置。
The third heat exchanger and the second heat exchanger are arranged in the air supply path such that at least part of the air flowing in the air supply path passes only through the second heat exchanger.
The air conditioner according to any one of claims 1 to 7.
 前記第3熱交換器は、前記第2熱交換器に対して鉛直方向の上側に配置される、
 請求項1~8のいずれか1項に記載の空気調和装置。
The third heat exchanger is arranged vertically above the second heat exchanger,
The air conditioner according to any one of claims 1 to 8.
 前記第3熱交換器と前記圧縮機との間に配置され、前記除湿運転モード時に液冷媒を貯留するアキュムレータを備えた、
 請求項1~9のいずれか1項に記載の空気調和装置。
An accumulator disposed between the third heat exchanger and the compressor for storing liquid refrigerant during the dehumidifying operation mode,
The air conditioner according to any one of claims 1 to 9.
PCT/JP2021/004555 2021-02-08 2021-02-08 Air-conditioning device Ceased WO2022168305A1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
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US12169085B2 (en) 2019-07-15 2024-12-17 Climate Master, Inc. Air conditioning system with capacity control and controlled hot water generation
US12181194B2 (en) 2016-07-08 2024-12-31 Climate Master, Inc. Heat pump and water heater
US12181179B2 (en) 2016-11-09 2024-12-31 Climate Master, Inc. Hybrid heat pump with improved dehumidification
US12181189B2 (en) 2021-11-10 2024-12-31 Climate Master, Inc. Ceiling-mountable heat pump system

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JP2013047590A (en) * 2011-08-29 2013-03-07 Chofu Seisakusho Co Ltd Desiccant ventilation fan

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JP2005147484A (en) * 2003-11-14 2005-06-09 Hitachi Ltd Air conditioner
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JP2012202680A (en) * 2011-03-28 2012-10-22 Tokyo Electric Power Co Inc:The Air conditioner
JP2013047590A (en) * 2011-08-29 2013-03-07 Chofu Seisakusho Co Ltd Desiccant ventilation fan

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Publication number Priority date Publication date Assignee Title
US12181194B2 (en) 2016-07-08 2024-12-31 Climate Master, Inc. Heat pump and water heater
US12181179B2 (en) 2016-11-09 2024-12-31 Climate Master, Inc. Hybrid heat pump with improved dehumidification
US12169085B2 (en) 2019-07-15 2024-12-17 Climate Master, Inc. Air conditioning system with capacity control and controlled hot water generation
US12173940B2 (en) 2019-07-15 2024-12-24 Climate Master, Inc. Air conditioning system with capacity control and controlled hot water generation
US12181189B2 (en) 2021-11-10 2024-12-31 Climate Master, Inc. Ceiling-mountable heat pump system

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