[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JP6309739B2 - Air conditioner - Google Patents

Air conditioner Download PDF

Info

Publication number
JP6309739B2
JP6309739B2 JP2013226643A JP2013226643A JP6309739B2 JP 6309739 B2 JP6309739 B2 JP 6309739B2 JP 2013226643 A JP2013226643 A JP 2013226643A JP 2013226643 A JP2013226643 A JP 2013226643A JP 6309739 B2 JP6309739 B2 JP 6309739B2
Authority
JP
Japan
Prior art keywords
refrigerant
receiver
flow rate
amount
rate adjusting
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.)
Active
Application number
JP2013226643A
Other languages
Japanese (ja)
Other versions
JP2015087065A (en
Inventor
円 上野
円 上野
田中 慎一
慎一 田中
野衣 浅地
野衣 浅地
昭 杉山
昭 杉山
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.)
Sharp Corp
Original Assignee
Sharp 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 Sharp Corp filed Critical Sharp Corp
Priority to JP2013226643A priority Critical patent/JP6309739B2/en
Priority to PCT/JP2014/071045 priority patent/WO2015064172A1/en
Publication of JP2015087065A publication Critical patent/JP2015087065A/en
Application granted granted Critical
Publication of JP6309739B2 publication Critical patent/JP6309739B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • 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
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • 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
    • F24F11/83Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers
    • F24F11/84Control systems characterised by their outputs; Constructional details thereof for controlling the temperature of the supplied air by controlling the supply of heat-exchange fluids to heat-exchangers using valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/39Dispositions with two or more expansion means arranged in series, i.e. multi-stage expansion, on a refrigerant line leading to the same evaporator
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B45/00Arrangements for charging or discharging refrigerant
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/006Compression machines, plants or systems with reversible cycle not otherwise provided for two pipes connecting the outdoor side to the indoor side with multiple indoor units
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2345/00Details for charging or discharging refrigerants; Service stations therefor
    • F25B2345/002Collecting refrigerant from a cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16Receivers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2523Receiver valves

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Air Conditioning Control Device (AREA)

Description

本発明は、冷媒を溜めるレシーバを利用して、冷媒回路を流れる冷媒量を調整する空気調和機に関する。   The present invention relates to an air conditioner that adjusts the amount of refrigerant flowing through a refrigerant circuit using a receiver that accumulates refrigerant.

空気調和機において、圧縮機、四方弁、凝縮器、絞り装置、蒸発器が順に配管により接続され、冷媒が循環する冷媒回路が形成される。特許文献1に記載された空気調和機では、凝縮器と蒸発器との間に、冷媒を溜めるレシーバが設けられ、レシーバの前後に高圧側絞り装置と低圧側絞り装置とが接続される。冷媒回路を循環する冷媒の状態量が目標値になるように、各絞り装置の開口面積が制御される。   In an air conditioner, a compressor, a four-way valve, a condenser, a throttling device, and an evaporator are sequentially connected by a pipe to form a refrigerant circuit in which refrigerant circulates. In the air conditioner described in Patent Document 1, a receiver for storing refrigerant is provided between a condenser and an evaporator, and a high-pressure side throttle device and a low-pressure side throttle device are connected before and after the receiver. The opening area of each expansion device is controlled so that the state quantity of the refrigerant circulating in the refrigerant circuit becomes a target value.

上記の空気調和機において、凝縮器で凝縮された冷媒は、高圧側絞り装置で減圧されて、レシーバに流入する。そして、レシーバから排出された冷媒は低圧側絞り装置で減圧されて、蒸発器へ供給される。レシーバに余剰の冷媒が溜められ、過熱度などの冷媒の状態量が制御される。   In the above air conditioner, the refrigerant condensed by the condenser is decompressed by the high pressure side expansion device and flows into the receiver. And the refrigerant | coolant discharged | emitted from the receiver is pressure-reduced with a low voltage | pressure side expansion apparatus, and is supplied to an evaporator. Excess refrigerant is stored in the receiver, and the state quantity of the refrigerant such as the degree of superheat is controlled.

特開平10−89780号公報Japanese Patent Laid-Open No. 10-89780

上記の空気調和機では、冷媒回路に1つのレシーバが存在している。このレシーバに冷媒を溜めたり、レシーバから冷媒を抜いたりすることにより、冷媒回路を循環する冷媒量が調整される。空調運転が行われるときの最適な冷媒量は、運転モード、外気温、室温などの運転状況によって異なる。しかし、レシーバが1つの場合、冷媒量の調整はレシーバの容積に制限され、最適な冷媒量に調整することができない場合がある。   In the above air conditioner, there is one receiver in the refrigerant circuit. The amount of refrigerant circulating in the refrigerant circuit is adjusted by accumulating the refrigerant in the receiver or removing the refrigerant from the receiver. The optimum amount of refrigerant when the air-conditioning operation is performed varies depending on operation conditions such as the operation mode, the outside air temperature, and the room temperature. However, when there is one receiver, the adjustment of the refrigerant amount is limited to the volume of the receiver and may not be adjusted to the optimum refrigerant amount.

本発明は、上記に鑑み、空調運転の運転状況に応じて、冷媒回路を循環する冷媒量を最適な冷媒量に調整することができる空気調和機の提供を目的とする。   In view of the above, an object of the present invention is to provide an air conditioner that can adjust the amount of refrigerant circulating in the refrigerant circuit to an optimum amount of refrigerant according to the operating state of the air conditioning operation.

本発明の空気調和機は、圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成されたものである。   The air conditioner of the present invention includes a refrigerant circuit in which a compressor, a condenser, a throttle unit, and an evaporator are connected by piping, and the throttle unit includes a plurality of receivers that store the refrigerant, and an amount of refrigerant that circulates through the refrigerant circuit. And a plurality of flow rate adjusting devices for adjusting the amount of refrigerant stored in each receiver in order to adjust the flow rate.

運転状況に応じて流量調整装置が動作すると、各レシーバに溜まる冷媒量が調整される。これにより、冷媒回路を循環する冷媒量が変化し、運転状況に応じた最適な冷媒量となる。   When the flow rate adjusting device operates according to the operating condition, the amount of refrigerant accumulated in each receiver is adjusted. Thereby, the amount of refrigerant circulating through the refrigerant circuit changes, and the optimum amount of refrigerant according to the operating situation is obtained.

冷媒回路に複数の流量調整装置が直列に配され、隣り合う流量調整装置の間にレシーバが接続され、レシーバよりも冷媒の流れ方向の下流側に位置する流量調整装置が動作することにより、レシーバに溜まる冷媒量が変化する。   A plurality of flow control devices are arranged in series in the refrigerant circuit, a receiver is connected between adjacent flow control devices, and the flow control device located downstream of the receiver in the flow direction of the refrigerant operates, thereby receiving the receiver. The amount of refrigerant that accumulates in the refrigerant changes.

冷媒回路を循環する冷媒が少なくなるように流量調整装置が動作すると、冷媒の流れ方向において、この流量調整装置の上流側に位置するレシーバに冷媒が溜まる。冷媒回路を循環する冷媒が多くなるように流量調整装置が動作すると、この流量調整装置の上流側に位置するレシーバに溜まっている冷媒が排出される。冷媒の流れ方向において、流量調整装置の下流側に位置するレシーバには、冷媒は溜まらない。このように、複数の流量調整装置を動作させることにより、レシーバ毎に溜まる冷媒量を調整することができる。   When the flow rate adjusting device operates so that the refrigerant circulating in the refrigerant circuit decreases, the refrigerant accumulates in the receiver positioned upstream of the flow rate adjusting device in the flow direction of the refrigerant. When the flow rate adjusting device operates so that more refrigerant circulates in the refrigerant circuit, the refrigerant accumulated in the receiver positioned upstream of the flow rate adjusting device is discharged. In the flow direction of the refrigerant, the refrigerant does not accumulate in the receiver located on the downstream side of the flow rate adjusting device. Thus, the refrigerant | coolant amount collected for every receiver can be adjusted by operating a some flow control apparatus.

流量調整装置の開度を制御する制御装置が設けられ、制御装置は、少なくとも1つの流量調整装置の開度を制御し、他の流量調整装置を全開にする。流量調整装置の開度の大小によって、流量調整装置を通過する冷媒量が変化し、レシーバに溜まる冷媒量が調整可能となる。1つあるいは複数の流量調整装置の開度を制御することにより、冷媒が溜まるレシーバの数が変わり、レシーバに溜まる冷媒量を調整することができる。   A control device for controlling the opening degree of the flow rate adjusting device is provided, and the control device controls the opening degree of at least one flow rate adjusting device and fully opens the other flow rate adjusting device. Depending on the degree of opening of the flow rate adjusting device, the amount of refrigerant passing through the flow rate adjusting device changes, and the amount of refrigerant accumulated in the receiver can be adjusted. By controlling the opening degree of one or a plurality of flow rate adjusting devices, the number of receivers in which the refrigerant accumulates changes, and the amount of refrigerant that accumulates in the receivers can be adjusted.

各レシーバの容積は同じとされるが、少なくとも1つのレシーバの容積は異なるようにした方がよい。冷媒を溜めるレシーバの組み合わせにより、全レシーバに溜めることができる冷媒量を調整でき、運転状況に応じて循環する冷媒量をより適切に調整することができる。   The volume of each receiver is the same, but the volume of at least one receiver should be different. The amount of refrigerant that can be accumulated in all receivers can be adjusted by the combination of receivers that accumulate refrigerant, and the amount of refrigerant that circulates can be adjusted more appropriately according to the operating conditions.

空気調和機が室内熱交換器を備えた室内機と室外熱交換器を備えた室外機とから構成されている場合、室内熱交換器の容積が室外熱交換器の容積よりも小さいとき、室外熱交換器に近いレシーバの容積が室内熱交換器に近いレシーバの容積より小さくされ、室外熱交換器の容積が室内熱交換器の容積よりも小さいとき、室外熱交換器に近いレシーバの容積が室内熱交換器に近いレシーバの容積より大きくされる。これにより、冷媒回路を循環する冷媒量が多くなり過ぎることを防げる。   When the air conditioner is composed of an indoor unit having an indoor heat exchanger and an outdoor unit having an outdoor heat exchanger, the outdoor heat exchanger has a volume smaller than that of the outdoor heat exchanger. When the volume of the receiver near the heat exchanger is smaller than the volume of the receiver near the indoor heat exchanger, and the volume of the outdoor heat exchanger is smaller than the volume of the indoor heat exchanger, the volume of the receiver near the outdoor heat exchanger is It is made larger than the volume of the receiver close to the indoor heat exchanger. Thereby, it can prevent that the refrigerant | coolant amount which circulates through a refrigerant circuit increases too much.

複数の流量調整装置の開度が所定の開度以上になったとき、制御装置は、圧縮機の回転数を下げる。冷媒回路を循環する冷媒が複数の流量調整装置を通過するとき、冷媒に圧力損失が生じる。そのため、流量調整装置を全開近くまで開いても、循環する冷媒量を多くことができず、冷媒不足となる。そこで、圧縮機の回転数が下げられると、回転数に応じた最適な冷媒量が少なくなるのに伴って、圧力損失が低下する。これにより、流量調整装置が全開近くまで開かなくても、流量調整装置を制御可能な範囲で運転することが可能となり、冷媒不足を解消できる。   When the opening degree of the plurality of flow rate adjusting devices becomes equal to or larger than the predetermined opening degree, the control device decreases the rotational speed of the compressor. When the refrigerant circulating in the refrigerant circuit passes through the plurality of flow control devices, a pressure loss occurs in the refrigerant. Therefore, even if the flow rate adjusting device is opened to near full open, the amount of circulating refrigerant cannot be increased, resulting in insufficient refrigerant. Therefore, when the rotational speed of the compressor is lowered, the pressure loss is reduced as the optimum amount of refrigerant corresponding to the rotational speed decreases. This makes it possible to operate the flow rate adjusting device within a controllable range without opening the flow rate adjusting device to near full open, thereby eliminating the shortage of refrigerant.

制御装置は、複数の流量調整装置の開度を所定の開度以上にして圧縮機の回転数を下げたとき、凝縮器に向かって送風するファンの回転数を下げる。複数の流量調整装置の開度が所定の開度以上になると、上記のように冷媒不足が生じる。凝縮器用のファンの回転数が下げられることにより、凝縮器の熱交換能力が低下し、ガス冷媒が流量調整装置を通過する。そのため、冷媒はレシーバに溜まらず、圧縮機の回転数だけを下げた場合に比べて、循環する冷媒量をより多くすることができる。   The control device lowers the rotational speed of the fan that blows air toward the condenser when the rotational speed of the compressor is lowered by setting the opening degree of the plurality of flow control devices to a predetermined opening degree or more. When the opening degree of the plurality of flow control devices is equal to or greater than the predetermined opening degree, the refrigerant shortage occurs as described above. By reducing the rotation speed of the condenser fan, the heat exchange capacity of the condenser is reduced, and the gas refrigerant passes through the flow rate adjusting device. Therefore, the refrigerant does not accumulate in the receiver, and the amount of refrigerant that circulates can be increased as compared with the case where only the rotation speed of the compressor is lowered.

冷媒回路から低温の冷媒を分流させてレシーバを冷却する冷却管と、冷媒回路から高温の冷媒を分流させてレシーバを温める加熱管とが設けられる。低温の冷媒によりレシーバが冷却されると、レシーバ内の冷媒が液化するので、レシーバに冷媒が流入しやすくなり、冷媒がレシーバに溜まる。高温の冷媒によりレシーバを温めると、レシーバ内の冷媒が蒸発するので、冷媒がレシーバから排出されやすくなり、レシーバ内の冷媒が減る。   A cooling pipe that cools the receiver by diverting a low-temperature refrigerant from the refrigerant circuit and a heating pipe that warms the receiver by diverting a high-temperature refrigerant from the refrigerant circuit are provided. When the receiver is cooled by the low-temperature refrigerant, the refrigerant in the receiver is liquefied, so that the refrigerant easily flows into the receiver, and the refrigerant accumulates in the receiver. When the receiver is warmed by the high-temperature refrigerant, the refrigerant in the receiver evaporates, so that the refrigerant is easily discharged from the receiver, and the refrigerant in the receiver is reduced.

レシーバが複数のタンクから構成される。小型のタンクを用いることができるので、小さな隙間にタンクを配置することが可能となり、レシーバの配置の自由度が増す。   The receiver is composed of a plurality of tanks. Since a small tank can be used, the tank can be arranged in a small gap, and the degree of freedom of arrangement of the receiver is increased.

冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置の開度を制御する制御装置が設けられ、制御装置は、圧縮機の吐出温度の変化を表す数式を用いて冷凍サイクルが安定したか否かを判断し、冷凍サイクルが安定してから流量調整装置の開度の制御を行う。   A control device for controlling the opening degree of the flow rate adjusting device is provided so that the refrigerant amount circulating in the refrigerant circuit becomes an optimum refrigerant amount according to the air conditioning operation, and the control device is a mathematical expression representing a change in the discharge temperature of the compressor. Is used to determine whether or not the refrigeration cycle is stable, and after the refrigeration cycle is stabilized, the opening degree of the flow control device is controlled.

上記の数式を用いることにより、冷凍サイクルが安定するタイミングを精度よく判断することができる。冷凍サイクルが安定してから流量調整装置の開度が制御され、循環する冷媒量を効率よく調整することができる。   By using the above formula, it is possible to accurately determine the timing at which the refrigeration cycle is stabilized. After the refrigeration cycle is stabilized, the opening degree of the flow rate adjusting device is controlled, and the circulating refrigerant amount can be adjusted efficiently.

本発明によると、複数のレシーバを用いて冷媒を溜めることにより、循環する冷媒量を運転状況に応じた最適な冷媒量にすることができ、効率よく空調運転を行える。   According to the present invention, by accumulating refrigerant using a plurality of receivers, the amount of refrigerant circulating can be set to the optimum refrigerant amount according to the operation status, and air conditioning operation can be performed efficiently.

本発明の第1の実施形態の空気調和機の冷媒回路を示す図The figure which shows the refrigerant circuit of the air conditioner of the 1st Embodiment of this invention. 第1の実施形態の冷房運転時の冷凍サイクルを示す図The figure which shows the refrigerating cycle at the time of the air_conditionaing | cooling operation of 1st Embodiment. 複数のレシーバが配置された室外機の内部を示す図The figure which shows the inside of the outdoor unit in which a plurality of receivers are arranged 室外機におけるレシーバの配置図Receiver layout in outdoor unit 空気調和機の制御ブロック図Air conditioner control block diagram 第3の実施形態の空気調和機の冷媒回路を示す図The figure which shows the refrigerant circuit of the air conditioner of 3rd Embodiment. 第3の実施形態の冷房運転時の冷凍サイクルを示す図The figure which shows the refrigerating cycle at the time of the air_conditionaing | cooling operation of 3rd Embodiment. 第3の実施形態の暖房運転時の冷凍サイクルを示す図The figure which shows the refrigerating cycle at the time of the heating operation of 3rd Embodiment. 第6の実施形態の冷凍サイクルを示す図The figure which shows the refrigerating cycle of 6th Embodiment. 流量調整装置が全開近くにあるときの制御フローチャートControl flow chart when the flow control device is near full open 流量調整装置が全開近くにあるときの制御フローチャートControl flow chart when the flow control device is near full open 第7の実施形態の露付き防止の制御フローチャートControl flowchart of prevention of dew condensation according to seventh embodiment 第8の実施形態の冷却管および加熱管が巻き付けられたレシーバを示す図The figure which shows the receiver by which the cooling tube and heating tube of 8th Embodiment were wound 第8の実施形態の冷凍サイクルを示す図The figure which shows the refrigerating cycle of 8th Embodiment. 第9の実施形態の冷凍サイクルを示す図The figure which shows the refrigerating cycle of 9th Embodiment 複数のタンクが配置された室外機の内部を示す図The figure which shows the inside of the outdoor unit where a plurality of tanks are arranged 複数のタンクから構成されたレシーバを示す図Diagram showing receiver composed of multiple tanks 他の形態のタンクを示す図The figure which shows the tank of other forms 第10の実施形態の冷凍サイクルの安定性判断のフローチャートFlowchart of refrigeration cycle stability determination of tenth embodiment (a)は圧縮機の回転数毎の吐出温度の時間変化を示す図、(b)はパラメータ毎の吐出温度の飽和曲線を示す図、(c)を圧縮機の回転数に応じて吐出温度の飽和曲線が変化することを示す図(A) is a figure which shows the time change of the discharge temperature for every rotation speed of a compressor, (b) is a figure which shows the saturation curve of the discharge temperature for every parameter, (c) is discharge temperature according to the rotation speed of a compressor. Showing that the saturation curve changes (d)は外気温に応じて吐出温度の飽和曲線が変化することを示す図、(e)は吐出温度の時間変化の近似式を示す図(D) is a figure which shows that the saturation curve of discharge temperature changes according to outside air temperature, (e) is a figure which shows the approximate expression of the time change of discharge temperature.

(第1の実施形態)
本実施形態の空気調和機は、図1に示すように、圧縮機1、凝縮器2、絞り部3、蒸発器4を配管で接続した冷媒回路を備えている。絞り部3は、冷媒を溜める複数のレシーバ5と、冷媒回路を循環する冷媒量を調整する複数の流量調整装置6とから構成される。
(First embodiment)
As shown in FIG. 1, the air conditioner of this embodiment includes a refrigerant circuit in which a compressor 1, a condenser 2, a throttle unit 3, and an evaporator 4 are connected by piping. The throttle unit 3 includes a plurality of receivers 5 that store refrigerant and a plurality of flow rate adjusting devices 6 that adjust the amount of refrigerant circulating in the refrigerant circuit.

レシーバ5は、1つの出入口を備えている。冷媒回路中の凝縮器2と蒸発器4とをつなぐ接続配管7から分岐した連結管8がレシーバ5の出入口に接続される。流量調整装置6は、膨張弁とされ、冷媒回路を循環する冷媒の流量および圧力を調整する。   The receiver 5 has one entrance. A connecting pipe 8 branched from a connecting pipe 7 that connects the condenser 2 and the evaporator 4 in the refrigerant circuit is connected to the inlet / outlet of the receiver 5. The flow rate adjusting device 6 is an expansion valve and adjusts the flow rate and pressure of the refrigerant circulating in the refrigerant circuit.

本実施形態では、3つのレシーバ5A,5B,5Cと2つの流量調整装置6A,6Bが冷媒の流れ方向に沿って交互に配される。高圧側流量調整装置6Aと低圧側流量調整装置6Bが冷媒回路に直列に並べられる。高圧側流量調整装置6Aは、低圧側流量調整装置6Bよりも冷媒の流れ方向の上流側に位置する。第1レシーバ5Aが凝縮器2と高圧側流量調整装置6Aとの間、第2レシーバ5Bが高圧側流量調整装置6Aと低圧側流量調整装置6Bとの間、第3レシーバ5Cが低圧側流量調整装置6Bと蒸発器4との間にそれぞれ接続される。   In the present embodiment, three receivers 5A, 5B, 5C and two flow rate adjusting devices 6A, 6B are alternately arranged along the flow direction of the refrigerant. The high pressure side flow rate adjustment device 6A and the low pressure side flow rate adjustment device 6B are arranged in series in the refrigerant circuit. The high pressure side flow rate adjustment device 6A is located upstream of the low pressure side flow rate adjustment device 6B in the refrigerant flow direction. The first receiver 5A is between the condenser 2 and the high pressure side flow rate adjustment device 6A, the second receiver 5B is between the high pressure side flow rate adjustment device 6A and the low pressure side flow rate adjustment device 6B, and the third receiver 5C is the low pressure side flow rate adjustment device. Each is connected between the device 6B and the evaporator 4.

本空気調和機は、室内機10と室外機11とからなるセパレートタイプである。空気調和機は、冷房運転、暖房運転などの空調運転を行う。図2に示すように、冷媒回路に四方弁12が設けられる。室内機10に、室内熱交換器13が設けられ、室外機11に、圧縮機1、四方弁12、室外熱交換器14、2つの流量調整装置6a,6bおよび3つのレシーバ5a,5b,5cが設けられる。また、室外機11に、室外熱交換器用のファン15が設けられ、室内機10に、室内熱交換器用のファン16が設けられる。なお、図中、17は冷媒の充填時などに使用する二方弁、18は同じく三方弁、19はバイパス配管用の二方弁である。   This air conditioner is a separate type composed of an indoor unit 10 and an outdoor unit 11. The air conditioner performs air conditioning operations such as cooling operation and heating operation. As shown in FIG. 2, a four-way valve 12 is provided in the refrigerant circuit. The indoor unit 10 is provided with an indoor heat exchanger 13, and the outdoor unit 11 includes a compressor 1, a four-way valve 12, an outdoor heat exchanger 14, two flow rate adjusting devices 6 a and 6 b, and three receivers 5 a, 5 b and 5 c. Is provided. The outdoor unit 11 is provided with an outdoor heat exchanger fan 15, and the indoor unit 10 is provided with an indoor heat exchanger fan 16. In the figure, 17 is a two-way valve used for charging refrigerant, 18 is a three-way valve, and 19 is a two-way valve for bypass piping.

圧縮機1から吐出された冷媒が、凝縮器2、絞り部3、蒸発器4を経て圧縮機1に戻る。このように冷媒が冷媒回路を循環する冷凍サイクルが形成される。図2の空気調和機において、四方弁12により、空調運転の運転モードに応じて冷媒の流れ方向が切り替えられる。   The refrigerant discharged from the compressor 1 returns to the compressor 1 through the condenser 2, the throttle unit 3, and the evaporator 4. In this way, a refrigeration cycle is formed in which the refrigerant circulates through the refrigerant circuit. In the air conditioner of FIG. 2, the flow direction of the refrigerant is switched by the four-way valve 12 according to the operation mode of the air conditioning operation.

冷房モードあるいは除霜モードのとき、室内熱交換器13が蒸発器4となり、室外熱交換器14が凝縮器2となる。第1流量調整装置6aが高圧側流量調整装置6A、第2流量調整装置6bが低圧側流量調整装置6Bとなる。レシーバ5aがレシーバ5A、レシーバ5bがレシーバ5B、レシーバ5cがレシーバ5Cに対応する。   In the cooling mode or the defrosting mode, the indoor heat exchanger 13 becomes the evaporator 4 and the outdoor heat exchanger 14 becomes the condenser 2. The first flow rate adjusting device 6a is the high pressure side flow rate adjusting device 6A, and the second flow rate adjusting device 6b is the low pressure side flow rate adjusting device 6B. The receiver 5a corresponds to the receiver 5A, the receiver 5b corresponds to the receiver 5B, and the receiver 5c corresponds to the receiver 5C.

暖房モードのときには、冷媒の流れ方向が逆となり、室内熱交換器13が凝縮器2となり、室外熱交換器14が蒸発器4となる。第2流量調整装置6bが高圧側流量調整装置6A、第1流量調整装置6aが低圧側流量調整装置6Bとなる。レシーバ5cがレシーバ5A、レシーバ5bがレシーバ5B、レシーバ5aがレシーバ5Cに対応する。   In the heating mode, the flow direction of the refrigerant is reversed, the indoor heat exchanger 13 becomes the condenser 2, and the outdoor heat exchanger 14 becomes the evaporator 4. The second flow rate adjusting device 6b is the high pressure side flow rate adjusting device 6A, and the first flow rate adjusting device 6a is the low pressure side flow rate adjusting device 6B. The receiver 5c corresponds to the receiver 5A, the receiver 5b corresponds to the receiver 5B, and the receiver 5a corresponds to the receiver 5C.

レシーバ5は、円筒状の容器であり、各レシーバ5の容積および形状は同じである。レシーバ5の底面に出入口が形成され、出入口は下向きとされる。レシーバ5は、室外熱交換器14と室内熱交換器13とをつなぐ接続配管7および各流量調整装置6よりも上方に位置する。連結管8は、接続配管7よりも小径とされ、接続配管7から上方に延びるように設けられる。連結管8の上部がレシーバ5の底面に接続され、下部が接続配管7に接続される。連結管8と接続配管7とは逆T形に接続された構造となる。   The receiver 5 is a cylindrical container, and the volume and shape of each receiver 5 are the same. An entrance / exit is formed on the bottom surface of the receiver 5, and the entrance / exit is directed downward. The receiver 5 is positioned above the connection pipe 7 that connects the outdoor heat exchanger 14 and the indoor heat exchanger 13 and the flow rate adjusting devices 6. The connecting pipe 8 has a smaller diameter than the connection pipe 7 and is provided so as to extend upward from the connection pipe 7. The upper part of the connecting pipe 8 is connected to the bottom surface of the receiver 5, and the lower part is connected to the connecting pipe 7. The connection pipe 8 and the connection pipe 7 are connected in an inverted T shape.

室外機11に設けられたレシーバ5は、室外熱交換器14の近傍に配置される。図3、図4に示すように、室外熱交換器14は室外機11の背面側に配置され、室外熱交換器14の左右方向の一側に、接続配管7を含む冷媒回路の配管や弁などの部品が配置される。それぞれの部品の間に隙間が形成される。各レシーバ5は、室外機11内の一側に配され、部品の隙間に配置される。レシーバ5が室外機11の背面側に配置されるので、太陽熱の影響を受けにくく、レシーバ5が高温になりにくい。   The receiver 5 provided in the outdoor unit 11 is disposed in the vicinity of the outdoor heat exchanger 14. As shown in FIGS. 3 and 4, the outdoor heat exchanger 14 is arranged on the back side of the outdoor unit 11, and a refrigerant circuit pipe or valve including a connection pipe 7 is provided on one side of the outdoor heat exchanger 14 in the left-right direction. Such parts are arranged. A gap is formed between each part. Each receiver 5 is arranged on one side in the outdoor unit 11 and arranged in a gap between components. Since the receiver 5 is arrange | positioned at the back side of the outdoor unit 11, it is hard to receive the influence of a solar heat and the receiver 5 does not become high temperature easily.

圧縮機1の吐出側と室外熱交換器14とを接続する配管は、室外機11の背面側を通り、他の配管よりも大径とされる。この大径の配管に、各レシーバ5が取り付けられる。各レシーバ5は、大径の配管以外の他の配管から離されて配される。各レシーバ5は他の配管や部品と接触しない。   A pipe connecting the discharge side of the compressor 1 and the outdoor heat exchanger 14 passes through the back side of the outdoor unit 11 and has a larger diameter than other pipes. Each receiver 5 is attached to this large-diameter pipe. Each receiver 5 is arranged separately from other pipes other than the large-diameter pipe. Each receiver 5 does not come into contact with other pipes or parts.

レシーバ5の固定方法として、レシーバ5が配管にろう付けされる、あるいはバンドなどの結束部材によりレシーバ5が配管に固定される。各レシーバ5は互いに接触しないように固定される。冷房モード時に、この配管に、高温高圧のガス冷媒が安定した状態で流れるため、配管の振動が少ない。この配管にレシーバ5を固定することにより、レシーバ5の振動を抑制することができ、冷媒がレシーバ5に出入りする際の騒音をなくすことができる。また、レシーバ5や配管が振動しても、各レシーバ5は大径の配管以外の他の配管や部品には接触しないので、騒音は生じない。なお、室外機11内の隙間の形状は複雑であるので、隙間の形状に応じて、レシーバ5の形状を変えてもよい。ただし、レシーバ5の容積は変えない。   As a method of fixing the receiver 5, the receiver 5 is brazed to the pipe, or the receiver 5 is fixed to the pipe by a binding member such as a band. Each receiver 5 is fixed so as not to contact each other. Since the high-temperature and high-pressure gas refrigerant flows through this pipe in a stable state during the cooling mode, vibration of the pipe is small. By fixing the receiver 5 to this pipe, vibration of the receiver 5 can be suppressed, and noise when the refrigerant enters and exits the receiver 5 can be eliminated. Further, even if the receiver 5 or the pipe vibrates, each receiver 5 does not come into contact with other pipes or parts other than the large-diameter pipe, so that no noise is generated. Since the shape of the gap in the outdoor unit 11 is complicated, the shape of the receiver 5 may be changed according to the shape of the gap. However, the volume of the receiver 5 is not changed.

図5に示すように、空気調和機は、冷凍サイクルを制御して、空調運転を行う制御装置20を備えている。空気調和機には、凝縮器2の温度を検出する凝縮器温度センサ21、蒸発器4の温度を検出する蒸発器温度センサ22、圧縮機1から吐出された冷媒の吐出温度を検出する吐出温度センサ23、圧縮機1に吸入される冷媒のサクション温度を検出するサクション温度センサ24、室温センサ25、外気温センサ26が設けられる。制御装置20は、ユーザが所望した空調運転に応じて、これらの温度センサの出力に基づき、圧縮機1、ファン15,16、流量調整装置6の動作を制御して、冷凍サイクルを制御する。   As shown in FIG. 5, the air conditioner includes a control device 20 that controls the refrigeration cycle and performs an air conditioning operation. The air conditioner includes a condenser temperature sensor 21 that detects the temperature of the condenser 2, an evaporator temperature sensor 22 that detects the temperature of the evaporator 4, and a discharge temperature that detects the discharge temperature of the refrigerant discharged from the compressor 1. A sensor 23, a suction temperature sensor 24 for detecting the suction temperature of the refrigerant sucked into the compressor 1, a room temperature sensor 25, and an outside air temperature sensor 26 are provided. The control device 20 controls the refrigeration cycle by controlling the operations of the compressor 1, the fans 15, 16 and the flow rate adjusting device 6 based on the outputs of these temperature sensors according to the air conditioning operation desired by the user.

なお、制御装置20は、室内機10に設けられた室内制御部と、室外機11に設けられた室外制御部とから構成される。室内制御部と室外制御部とは互いに通信可能に接続され、両者が連携して室内機10および室外機11の動作を制御する。   The control device 20 includes an indoor control unit provided in the indoor unit 10 and an outdoor control unit provided in the outdoor unit 11. The indoor control unit and the outdoor control unit are connected so as to be communicable with each other, and both cooperate to control operations of the indoor unit 10 and the outdoor unit 11.

冷媒回路に設けられる複数の流量調整装置6は同じタイプの膨張弁とされる。この膨張弁は、0〜500段階の間で開度を可変できる。膨張弁では、開度に応じた開口面積となり、通過する冷媒量を可変することができる。したがって、各流量調整装置6の開度の大小は流量調整装置6を通過する冷媒量の大小に対応する。開度が大きくなるほど、通過する冷媒量は増える。   The plurality of flow rate adjusting devices 6 provided in the refrigerant circuit are the same type of expansion valve. The opening of the expansion valve can be varied between 0 and 500 steps. The expansion valve has an opening area corresponding to the opening, and the amount of refrigerant passing therethrough can be varied. Therefore, the magnitude of the opening degree of each flow rate adjustment device 6 corresponds to the magnitude of the refrigerant amount passing through the flow rate adjustment device 6. As the opening degree increases, the amount of refrigerant passing therethrough increases.

高圧側流量調整装置6Aおよび低圧側流量調整装置6Bの開度をそれぞれ変えることにより、各流量調整装置6A,6Bを通過する冷媒量が変化して、各流量調整装置6A,6Bの上流側と下流側とにおいて冷媒の圧力差が生じる。低圧側流量調整装置6Bの開度を高圧側流量調整装置6Aの開度より大きくすると、高圧側流量調整装置6Aの上流側の圧力が下流側の圧力より高くなる。高圧側流量調整装置6Aの上流側にある第1レシーバ5Aの連結管8に液冷媒が流れ込み、第1レシーバ5Aに液冷媒が溜まる。高圧側流量調整装置6Aの下流側にある第2レシーバ5Bおよび第3レシーバ5Cには、液冷媒は溜まらない。なお、第2レシーバ5B内の圧力が高圧側流量調整装置6Aと低圧側流量調整装置6Bとの間における冷媒の圧力より低い場合、その圧力差に応じて液冷媒が第2レシーバ5Bに流れ込んで溜まる。   By changing the opening degree of the high pressure side flow rate adjustment device 6A and the low pressure side flow rate adjustment device 6B, the amount of refrigerant passing through each flow rate adjustment device 6A, 6B changes, and the upstream side of each flow rate adjustment device 6A, 6B. A refrigerant pressure difference occurs between the downstream side and the downstream side. When the opening degree of the low pressure side flow rate adjustment device 6B is made larger than the opening degree of the high pressure side flow rate adjustment device 6A, the pressure on the upstream side of the high pressure side flow rate adjustment device 6A becomes higher than the pressure on the downstream side. The liquid refrigerant flows into the connecting pipe 8 of the first receiver 5A on the upstream side of the high-pressure side flow rate adjusting device 6A, and the liquid refrigerant accumulates in the first receiver 5A. Liquid refrigerant does not accumulate in the second receiver 5B and the third receiver 5C on the downstream side of the high-pressure side flow control device 6A. In addition, when the pressure in the 2nd receiver 5B is lower than the pressure of the refrigerant | coolant between the high pressure side flow volume adjustment apparatus 6A and the low pressure side flow volume adjustment apparatus 6B, a liquid refrigerant flows into the 2nd receiver 5B according to the pressure difference. Accumulate.

ここで、高圧側流量調整装置6Aの開度が大きくされると、高圧側流量調整装置6Aの上流側の圧力が低くなる。第1レシーバ5Aに溜まっている液冷媒が冷媒回路に排出される。   Here, when the opening degree of the high pressure side flow rate adjusting device 6A is increased, the pressure on the upstream side of the high pressure side flow rate adjusting device 6A becomes lower. The liquid refrigerant accumulated in the first receiver 5A is discharged to the refrigerant circuit.

高圧側流量調整装置6Aの開度を低圧側流量調整装置6Bの開度より大きくすると、低圧側流量調整装置6Bの上流側の圧力が下流側の圧力より高くなる。これにより、低圧側流量調整装置6Bの上流側にある第1レシーバ5Aおよび第2レシーバ5Bに液冷媒が溜まり、低圧側流量調整装置6Bの下流側にある第3レシーバ5Cには、液冷媒は溜まらない。   When the opening degree of the high pressure side flow rate adjustment device 6A is made larger than the opening degree of the low pressure side flow rate adjustment device 6B, the pressure on the upstream side of the low pressure side flow rate adjustment device 6B becomes higher than the pressure on the downstream side. As a result, liquid refrigerant accumulates in the first receiver 5A and the second receiver 5B on the upstream side of the low-pressure flow rate adjustment device 6B, and the liquid refrigerant is stored in the third receiver 5C on the downstream side of the low-pressure flow rate adjustment device 6B. I do not collect.

ここで、低圧側流量調整装置6Bの開度が大きくされると、低圧側流量調整装置6Bの上流側の圧力が低くなる。第1レシーバ5Aおよび第2レシーバ5Bに溜まっている液冷媒が冷媒回路に排出される。   Here, when the opening degree of the low pressure side flow rate adjusting device 6B is increased, the pressure on the upstream side of the low pressure side flow rate adjusting device 6B becomes low. The liquid refrigerant accumulated in the first receiver 5A and the second receiver 5B is discharged to the refrigerant circuit.

空調運転が行われるとき、制御装置20は、室温が設定温度になるように冷凍サイクルを制御する。このとき、制御装置20は、運転状況に応じて冷媒回路を循環する冷媒量が最適になるように冷媒量を調整する。冷媒回路に充填された冷媒の一部は、レシーバ5に溜められ、残りの冷媒が冷媒回路を循環する。循環する冷媒量のうち、COPが最大となるときの冷媒量が最適冷媒量とされる。最適冷媒量は、運転モードによって異なり、さらに圧縮機1の回転数、外気温、室温、室内外の熱交換器の容積によっても異なる。例えば、冷房モードにおいて、急速に冷やす急速冷房モード時には、より多くの冷媒が必要となる。   When the air conditioning operation is performed, the control device 20 controls the refrigeration cycle so that the room temperature becomes the set temperature. At this time, the control device 20 adjusts the amount of refrigerant so that the amount of refrigerant circulating through the refrigerant circuit is optimized in accordance with the operating conditions. A part of the refrigerant filled in the refrigerant circuit is accumulated in the receiver 5, and the remaining refrigerant circulates in the refrigerant circuit. Of the circulating refrigerant amount, the refrigerant amount when the COP is maximum is set as the optimum refrigerant amount. The optimum amount of refrigerant varies depending on the operation mode, and also varies depending on the rotation speed of the compressor 1, the outside air temperature, the room temperature, and the volume of the heat exchanger indoors and outdoors. For example, in the cooling mode, more refrigerant is required in the rapid cooling mode in which cooling is performed rapidly.

空調運転が開始されると、制御装置20は、設定温度と室温とに基づいて圧縮機1の目標回転数を設定し、目標回転数に応じて高圧側および低圧側流量調整装置6A,6Bの開度を決める。制御装置20は、決められた運転条件にしたがって圧縮機1、各流量調整装置6A,6B、ファン15,16などを制御する。また、制御装置20は、目標回転数および運転モード(冷房モード、暖房モードなど)に応じて各流量調整装置6A,6Bの初期開度を決める。   When the air-conditioning operation is started, the control device 20 sets the target rotational speed of the compressor 1 based on the set temperature and the room temperature, and the high-pressure side and low-pressure side flow control devices 6A and 6B according to the target rotational speed. Determine the opening. The control device 20 controls the compressor 1, the flow rate adjusting devices 6A and 6B, the fans 15 and 16, and the like according to the determined operating conditions. Moreover, the control apparatus 20 determines the initial opening degree of each flow volume adjustment apparatus 6A, 6B according to target rotation speed and operation modes (cooling mode, heating mode, etc.).

空気調和機が停止しているとき、高圧側および低圧側流量調整装置6A,6Bは、全開されている。空調運転が開始されると、制御装置20は、各流量調整装置6A,6Bのイニシャライズを行う。すなわち、各流量調整装置6A,6Bが一旦全閉された後、各流量調整装置6A,6Bはそれぞれ初期開度まで開かれる。この後、圧縮機1が起動され、冷媒が冷媒回路を循環する。   When the air conditioner is stopped, the high-pressure side and low-pressure side flow control devices 6A and 6B are fully opened. When the air conditioning operation is started, the control device 20 initializes the flow rate adjusting devices 6A and 6B. That is, after each flow rate adjusting device 6A, 6B is fully closed, each flow rate adjusting device 6A, 6B is opened to the initial opening degree. Thereafter, the compressor 1 is started and the refrigerant circulates through the refrigerant circuit.

ここで、空調運転の起動時に、制御装置20は、低圧側流量調整装置6Bの開度が高圧側流量調整装置6Aの開度よりも大きくなるように、各流量調整装置6A,6Bを動作させる。例えば、低圧側流量調整装置6Bが全開され、高圧側流量調整装置6Aが決められた初期開度にされる。この間、圧縮機1の回転数は一定とされる。第2レシーバ5Bに溜まっていた液冷媒が冷媒回路に流れ出す。また、高圧側流量調整装置6Aを開けることにより、上流側の第1レシーバ5Aに溜まっていた液冷媒の一部が冷媒回路に流れ出す。このように、冷媒回路を循環する冷媒が増えることにより、凝縮器2の出口側の過冷却が大きくなって、空調能力を高めることができる。暖房モードの場合、運転開始からより温度の高い温風を吹き出すことができる。   Here, at the time of starting the air conditioning operation, the control device 20 operates the flow rate adjusting devices 6A and 6B so that the opening degree of the low pressure side flow rate adjusting device 6B is larger than the opening degree of the high pressure side flow rate adjusting device 6A. . For example, the low pressure side flow rate adjustment device 6B is fully opened, and the high pressure side flow rate adjustment device 6A is set to the determined initial opening. During this time, the rotational speed of the compressor 1 is constant. The liquid refrigerant that has accumulated in the second receiver 5B flows out into the refrigerant circuit. Further, by opening the high-pressure flow rate adjusting device 6A, a part of the liquid refrigerant that has accumulated in the first receiver 5A on the upstream side flows out to the refrigerant circuit. As described above, when the refrigerant circulating in the refrigerant circuit is increased, the supercooling on the outlet side of the condenser 2 is increased, and the air conditioning capability can be enhanced. In the heating mode, warm air having a higher temperature can be blown out from the start of operation.

制御装置20は、空調運転の開始後に冷凍サイクルが安定したとき、循環する冷媒量が最適冷媒量となるように冷媒量調整制御を行う。冷凍サイクルの安定の判断は、圧縮機1から吐出される冷媒の温度によって行われる。制御装置20は、吐出温度センサ23の出力に基づいて吐出温度の変化を監視する。吐出温度の変化が小さくなったとき、制御装置20は、吐出温度が安定したことを認識し、冷凍サイクルが安定したと判断する。   When the refrigeration cycle is stabilized after the start of the air conditioning operation, the control device 20 performs refrigerant amount adjustment control so that the circulating refrigerant amount becomes the optimum refrigerant amount. The determination of the stability of the refrigeration cycle is made based on the temperature of the refrigerant discharged from the compressor 1. The control device 20 monitors the change in the discharge temperature based on the output of the discharge temperature sensor 23. When the change in the discharge temperature becomes small, the control device 20 recognizes that the discharge temperature is stable and determines that the refrigeration cycle is stable.

冷媒量調整制御では、運転モード、過熱度、圧縮機1の回転数、外気温、室温などの運転状況に応じて、高圧側および低圧側流量調整装置6A,6Bの開度が設定される。制御装置20は、冷媒量調整制御を行うとき、運転モード、外気温に基づいて圧縮機1の回転数を決め、この回転数に応じて最適な冷媒量を設定し、最適な冷媒量となるように各流量調整装置6A,6Bの開度を決める。そして、制御装置20は、決められた開度になるように各流量調整装置6A,6Bを制御する。なお、運転状況に応じた各流量調整装置6A,6Bの開度は、実験等により予め決められ、制御装置20のメモリに記憶されている。制御装置20は、空調運転中、現在の運転状況に応じた各流量調整装置6A,6Bの開度をメモリから読み出し、読み出した開度に応じて各流量調整装置6A,6Bを動作させる。   In the refrigerant amount adjustment control, the opening degrees of the high-pressure side and low-pressure side flow rate adjusting devices 6A and 6B are set according to the operation state such as the operation mode, the degree of superheat, the rotational speed of the compressor 1, the outside air temperature, and the room temperature. When the refrigerant amount adjustment control is performed, the control device 20 determines the number of rotations of the compressor 1 based on the operation mode and the outside air temperature, sets an optimum amount of refrigerant according to the number of revolutions, and becomes the optimum amount of refrigerant. In this way, the opening degree of each flow rate adjusting device 6A, 6B is determined. And the control apparatus 20 controls each flow volume adjustment apparatus 6A, 6B so that it may become the determined opening degree. Note that the opening degree of each of the flow rate adjusting devices 6A and 6B according to the operating condition is determined in advance by experiments or the like and stored in the memory of the control device 20. During the air conditioning operation, the control device 20 reads the opening amounts of the flow rate adjustment devices 6A and 6B according to the current operation state from the memory, and operates the flow rate adjustment devices 6A and 6B according to the read opening amounts.

制御装置20は、冷凍サイクルが安定したことを確認すると、設定された開度になるように高圧側および低圧側流量調整装置6A,6Bを動作させる。すなわち、一方の流量調整装置6が制御され、他方の流量調整装置6が全開とされる。各流量調整装置6A,6Bの動作順として、まず他方の流量調整装置6が全開され、次いで一方の流量調整装置6が設定された開度まで動作する。   When confirming that the refrigeration cycle is stable, the control device 20 operates the high-pressure side and low-pressure side flow rate adjustment devices 6A and 6B so that the set opening degree is obtained. That is, one flow rate adjusting device 6 is controlled and the other flow rate adjusting device 6 is fully opened. As the order of operation of the flow rate adjusting devices 6A and 6B, first, the other flow rate adjusting device 6 is fully opened, and then one flow rate adjusting device 6 operates to the set opening degree.

高圧側流量調整装置6Aの開度が設定された開度に制御され、低圧側流量調整装置6Bが全開されると、第1レシーバ5Aでは、液冷媒が流入して溜まる。第2、第3レシーバ5B,5Cには、液冷媒は溜まらない。すなわち、第2、第3レシーバ5B,5Cでは、冷媒は出入りしない、あるいは溜まっている液冷媒が排出される。   When the opening of the high-pressure flow rate adjusting device 6A is controlled to the set opening, and the low-pressure flow rate adjusting device 6B is fully opened, the liquid refrigerant flows in and accumulates in the first receiver 5A. Liquid refrigerant does not accumulate in the second and third receivers 5B and 5C. That is, in the second and third receivers 5B and 5C, the liquid refrigerant that does not enter or exit or that has accumulated is discharged.

また、低圧側流量調整装置6Bの開度が設定された開度に制御され、高圧側流量調整装置6Aが全開されると、第1、第2レシーバ5A,5Bでは、液冷媒が流入して溜まる。第3レシーバ5Cには、液冷媒は溜まらない。すなわち、第3レシーバ5Cでは、冷媒は出入りしない、あるいは溜まっている液冷媒が排出される。このように、レシーバ5よりも冷媒の流れ方向の下流側に位置する流量調整装置6を制御することにより、この流量調整装置6の上流側に位置するレシーバ5に溜まる冷媒量を調整することができる。   In addition, when the opening of the low-pressure flow rate adjusting device 6B is controlled to the set opening and the high-pressure flow adjusting device 6A is fully opened, liquid refrigerant flows into the first and second receivers 5A and 5B. Accumulate. Liquid refrigerant does not accumulate in the third receiver 5C. That is, in the third receiver 5C, the refrigerant does not enter or exit or the liquid refrigerant that has accumulated is discharged. In this way, by controlling the flow rate adjustment device 6 located downstream of the receiver 5 in the refrigerant flow direction, the amount of refrigerant accumulated in the receiver 5 located upstream of the flow rate adjustment device 6 can be adjusted. it can.

また、2つの流量調整装置6の開度を制御してもよい。低圧側流量調整装置6Bの開度が高圧側流量調整装置6Aの開度より大きくなるように制御されると、それぞれの流量調整装置6の上流側と下流側において、流れる冷媒に圧力差が生じる。第1レシーバ5Aに液冷媒が溜まるとともに、第2レシーバ5Bにも液冷媒が少し溜まる。高圧側流量調整装置6Aの開度が低圧側流量調整装置6Bの開度より大きくなるように制御されると、第2レシーバ5Bに液冷媒が溜まるとともに、第1レシーバ5Aにも液冷媒が少し溜まる。   Moreover, you may control the opening degree of the two flow volume adjustment apparatuses 6. FIG. When the opening degree of the low pressure side flow rate adjusting device 6B is controlled to be larger than the opening degree of the high pressure side flow rate adjusting device 6A, a pressure difference occurs between the refrigerant flowing on the upstream side and the downstream side of each flow rate adjusting device 6. . While the liquid refrigerant accumulates in the first receiver 5A, a little liquid refrigerant accumulates also in the second receiver 5B. When the opening of the high pressure side flow control device 6A is controlled to be larger than the opening of the low pressure flow control device 6B, liquid refrigerant accumulates in the second receiver 5B and a little liquid refrigerant also in the first receiver 5A. Accumulate.

したがって、各流量調整装置6を制御することにより、各レシーバ5に溜まる冷媒量が異なり、冷媒回路を循環する冷媒量を調整することが可能となる。そして、運転状況に応じた最適な冷媒量に容易にすることができる。これにより、空気調和機を効率的に運転することができ、消費電力の低減や運転能力の向上を図れる。   Therefore, by controlling each flow rate adjusting device 6, the amount of refrigerant accumulated in each receiver 5 is different, and the amount of refrigerant circulating in the refrigerant circuit can be adjusted. And it can be made easy to the optimal refrigerant | coolant amount according to a driving | running condition. As a result, the air conditioner can be operated efficiently, and power consumption can be reduced and operating capacity can be improved.

ここで、運転状況は変化していくので、制御装置20は、室温、外気温などに応じて圧縮機1の回転数を変える。圧縮機1の回転数の変化に伴って、最適な冷媒量は変化する。圧縮機1の回転数が上がると、最適な冷媒量は多くなり、圧縮機1の回転数が下がると、最適な冷媒量は少なくなる。   Here, since the operation state changes, the control device 20 changes the rotation speed of the compressor 1 according to the room temperature, the outside air temperature, and the like. The optimal amount of refrigerant changes as the rotational speed of the compressor 1 changes. When the rotation speed of the compressor 1 increases, the optimum refrigerant amount increases, and when the rotation speed of the compressor 1 decreases, the optimum refrigerant amount decreases.

冷媒回路を循環する冷媒量を多くする場合、制御装置20は、低圧側流量調整装置6Bを全開にし、高圧側流量調整装置6Aを制御する。第1レシーバ5Aでは、液冷媒が流入して溜まるが、第2、第3レシーバ5B,5Cでは、溜まっていた液冷媒が流れ出す。したがって、第1レシーバ5Aの容積に応じた冷媒量だけが溜まり、循環する冷媒量は多くなる。   When increasing the amount of refrigerant circulating through the refrigerant circuit, the control device 20 fully opens the low-pressure side flow rate adjustment device 6B and controls the high-pressure side flow rate adjustment device 6A. In the first receiver 5A, liquid refrigerant flows in and accumulates, but in the second and third receivers 5B and 5C, the accumulated liquid refrigerant flows out. Accordingly, only the refrigerant amount corresponding to the volume of the first receiver 5A is accumulated, and the circulating refrigerant amount is increased.

冷媒回路を循環する冷媒量を少なくする場合、制御装置20は、高圧側流量調整装置6Aを全開にし、低圧側流量調整装置6Bを制御する。第1、第2レシーバ5A,5Bでは、液冷媒が流入して溜まるが、第3レシーバ5Cでは、溜まっていた液冷媒が流れ出す。したがって、第1レシーバ5Aと第2レシーバ5Bとの合計容積に応じて冷媒が溜まり、循環する冷媒量は少なくなる。   When reducing the amount of refrigerant circulating in the refrigerant circuit, the control device 20 fully opens the high-pressure side flow rate adjustment device 6A and controls the low-pressure side flow rate adjustment device 6B. In the first and second receivers 5A and 5B, liquid refrigerant flows in and accumulates, but in the third receiver 5C, the accumulated liquid refrigerant flows out. Therefore, the refrigerant accumulates according to the total volume of the first receiver 5A and the second receiver 5B, and the amount of refrigerant circulating is reduced.

また、外気温や室温が変化すると、過熱度が変化する。制御装置20は、過熱度の変動に応じて各流量調整装置6の開度を制御する。なお、制御装置20は、蒸発器温度センサ22あるいはサクション温度センサ24によって検出された蒸発器4の温度に基づいて過熱度の変化を判断する。また、過熱度は、蒸発器4の入口側の温度と圧縮機1の吸入側の温度とに基づいて求めてもよい。   Further, when the outside air temperature or room temperature changes, the degree of superheat changes. The control device 20 controls the opening degree of each flow rate adjusting device 6 according to the change in the degree of superheat. The control device 20 determines a change in the degree of superheat based on the temperature of the evaporator 4 detected by the evaporator temperature sensor 22 or the suction temperature sensor 24. Further, the degree of superheat may be obtained based on the temperature on the inlet side of the evaporator 4 and the temperature on the suction side of the compressor 1.

過熱度が大きくなったとき、制御装置20は、一方の流量調整装置6の開度が大きくなるように制御する。例えば、高圧側流量調整装置6Aが制御されているとき、高圧側流量調整装置6Aの開度が大きくなると、第1レシーバ5Aに溜まっていた液冷媒が減る。蒸発器4を通過する冷媒が増えることにより、過熱度が小さくなる。また、過熱度が小さくなったとき、制御装置20は、一方の流量調整装置6の開度が小さくなるように制御する。例えば、高圧側流量調整装置6Aが制御されているとき、高圧側流量調整装置6Aの開度が小さくなると、第1レシーバ5Aに溜まる液冷媒が増える。蒸発器4を通過する冷媒が減ることにより、過熱度が大きくなる。   When the degree of superheat increases, the control device 20 performs control so that the opening degree of one flow rate adjustment device 6 is increased. For example, when the high pressure side flow rate adjustment device 6A is controlled, the liquid refrigerant accumulated in the first receiver 5A decreases when the opening of the high pressure side flow rate adjustment device 6A increases. As the refrigerant passing through the evaporator 4 increases, the degree of superheat decreases. Further, when the degree of superheat becomes small, the control device 20 performs control so that the opening degree of one flow rate adjustment device 6 becomes small. For example, when the high-pressure flow rate adjustment device 6A is controlled, the liquid refrigerant that accumulates in the first receiver 5A increases as the opening of the high-pressure flow rate adjustment device 6A decreases. As the refrigerant passing through the evaporator 4 decreases, the degree of superheat increases.

なお、上記の冷媒回路では、3つのレシーバ5と2つの流量調整装置6を有しているが、レシーバ5は、2つあるいは4つ以上であってもよい。2つのレシーバ5に対しては、2つあるいは3つの流量調整装置6が設けられる。4つのレシーバ5に対しては、3つ〜5つの流量調整装置6が設けられる。また、3つのレシーバ5に対しては、3つあるいは4つの流量調整装置6を設けてもよい。レシーバ5と流量調整装置6とは、冷媒の流れ方向において交互に配される。レシーバ5の数と流量調整装置6の数によって、制御可能な冷媒量を増減することが可能となる。数が多いほど、様々な冷媒量に調整が可能となる。   In the above refrigerant circuit, the three receivers 5 and the two flow rate adjusting devices 6 are provided, but the number of receivers 5 may be two or four or more. Two or three flow rate adjusting devices 6 are provided for the two receivers 5. Three to five flow rate adjusting devices 6 are provided for the four receivers 5. Further, three or four flow rate adjusting devices 6 may be provided for the three receivers 5. The receiver 5 and the flow rate adjusting device 6 are alternately arranged in the flow direction of the refrigerant. The amount of refrigerant that can be controlled can be increased or decreased by the number of receivers 5 and the number of flow control devices 6. The larger the number, the more various refrigerant amounts can be adjusted.

(第2の実施形態)
第1の実施形態の空気調和機において、室内機10に設置される室内熱交換器13と室外機11に設置される室外熱交換器14とでは、容積が異なることがある。容積が異なることにより、運転モードに応じて最適な冷媒量も異なる。室外熱交換器14の容積が室内熱交換器13の容積より大のとき、冷房モード時の最適な冷媒量は暖房モード時の最適な冷媒量よりも大となる。室内熱交換器13の容積が室外熱交換器14の容積より大のとき、暖房モード時の最適な冷媒量は冷房モード時の最適な冷媒量よりも大となる。
(Second Embodiment)
In the air conditioner of the first embodiment, the indoor heat exchanger 13 installed in the indoor unit 10 and the outdoor heat exchanger 14 installed in the outdoor unit 11 may have different volumes. Due to the different volumes, the optimum refrigerant amount varies depending on the operation mode. When the volume of the outdoor heat exchanger 14 is larger than the volume of the indoor heat exchanger 13, the optimum refrigerant amount in the cooling mode is larger than the optimum refrigerant amount in the heating mode. When the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14, the optimum refrigerant amount in the heating mode is larger than the optimum refrigerant amount in the cooling mode.

室内外の熱交換器13,14の容積の大小に関する情報は、空気調和機の工場出荷時あるいは設置時に予め設定される。制御装置20は、この情報に基づいて、空調運転時に循環する冷媒量を多くするのか少なくするのかを決める。そして、制御装置20は、運転モードに応じた最適な冷媒量になるように、流量調整装置6を制御する。なお、室内外の熱交換器13,14を除くその他の構成および動作は、第1の実施形態と同じである。   Information on the size of the indoor and outdoor heat exchangers 13 and 14 is set in advance at the time of factory shipment or installation of the air conditioner. Based on this information, the control device 20 determines whether to increase or decrease the amount of refrigerant circulating during the air conditioning operation. And the control apparatus 20 controls the flow volume adjustment apparatus 6 so that it may become the optimal refrigerant | coolant amount according to an operation mode. The other configurations and operations except for the indoor and outdoor heat exchangers 13 and 14 are the same as those in the first embodiment.

すなわち、凝縮器2の容積が蒸発器4の容積より大のとき、制御装置20は、高圧側流量調整装置6Aを制御し、低圧側流量調整装置6Bを全開にする。第1レシーバ5Aに冷媒が溜まり、第2、第3レシーバ5B,5Cには冷媒は溜まらない。これにより、循環する冷媒量を多くすることができる。逆に、制御装置20は、低圧側流量調整装置6Bを制御し、高圧側流量調整装置6Aを全開にすると、第1、第2レシーバ5A,5Bに冷媒が溜まり、第3レシーバ5Cには冷媒は溜まらない。このとき、循環する冷媒量が少なくなる。   That is, when the volume of the condenser 2 is larger than the volume of the evaporator 4, the control device 20 controls the high pressure side flow rate adjustment device 6A and fully opens the low pressure side flow rate adjustment device 6B. The refrigerant accumulates in the first receiver 5A, and no refrigerant accumulates in the second and third receivers 5B and 5C. Thereby, the amount of circulating refrigerant can be increased. Conversely, when the control device 20 controls the low pressure side flow rate adjustment device 6B and fully opens the high pressure side flow rate adjustment device 6A, the refrigerant accumulates in the first and second receivers 5A and 5B, and the third receiver 5C receives the refrigerant. Will not accumulate. At this time, the amount of circulating refrigerant decreases.

ここで、冷房モード時には、室外熱交換器14が凝縮器2となり、室内熱交換器13が蒸発器4となる。暖房モード時には、室内熱交換器13が凝縮器2となり、室外熱交換器14が蒸発器4となる。いずれの運転モードでも、凝縮器2に近い側の流量調整装置6が制御され、蒸発器4に近い側の流量調整装置6が全開にされることにより、循環する冷媒量が多くなる。   Here, in the cooling mode, the outdoor heat exchanger 14 becomes the condenser 2 and the indoor heat exchanger 13 becomes the evaporator 4. In the heating mode, the indoor heat exchanger 13 becomes the condenser 2 and the outdoor heat exchanger 14 becomes the evaporator 4. In any operation mode, the flow rate adjusting device 6 on the side close to the condenser 2 is controlled, and the flow rate adjusting device 6 on the side close to the evaporator 4 is fully opened, so that the amount of the circulating refrigerant increases.

したがって、室内外の熱交換器13,14の容積に差があるとき、高圧側流量調整装置6Aを制御して、低圧側流量調整装置6Bを全開にすることにより、運転モードに応じた適切な量の冷媒を循環させることができ、効率のよい空調運転を行うことができる。一方で、冷房モード時と暖房モード時で冷媒回路を循環する冷媒の流れが逆になる。例えば図2に示す冷媒回路において、高圧側流量調整装置6aを制御して、低圧側流量調整装置6bを全開にすると、冷房モード時にレシーバ5aに液冷媒が溜まるとすると、暖房モード時にはレシーバ5b,5cに液冷媒が溜まる。このとき、室内熱交換器13の容積が室外熱交換器14の容積よりも小さい場合、レシーバ5aの容積はレシーバ5cの容積よりも小とするほうがよい。室外熱交換器14の容積が室内熱交換器13の容積よりも小さい場合、レシーバ5cの容積はレシーバ5aの容積よりも小とするほうがよい。このようにすることにより、冷媒過多の運転状態を避けやすく、最適な冷媒量での運転がしやすくなる。   Therefore, when there is a difference in the volume of the heat exchangers 13 and 14 indoors and outdoors, the high pressure side flow rate adjustment device 6A is controlled and the low pressure side flow rate adjustment device 6B is fully opened. An amount of refrigerant can be circulated, and efficient air-conditioning operation can be performed. On the other hand, the flow of the refrigerant circulating in the refrigerant circuit is reversed between the cooling mode and the heating mode. For example, in the refrigerant circuit shown in FIG. 2, if the high-pressure flow rate adjustment device 6a is controlled and the low-pressure flow rate adjustment device 6b is fully opened, the liquid refrigerant accumulates in the receiver 5a during the cooling mode. Liquid refrigerant accumulates in 5c. At this time, when the volume of the indoor heat exchanger 13 is smaller than the volume of the outdoor heat exchanger 14, the volume of the receiver 5a is preferably smaller than the volume of the receiver 5c. When the volume of the outdoor heat exchanger 14 is smaller than the volume of the indoor heat exchanger 13, the volume of the receiver 5c is preferably smaller than the volume of the receiver 5a. By doing so, it is easy to avoid an excessive refrigerant state, and it is easy to operate with an optimal amount of refrigerant.

図2に示す空気調和機において、室外熱交換器14の容積が室内熱交換器13の容積より大であるとき、冷房モード時には、制御装置20は、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にする。第1レシーバ5aだけに液冷媒が溜まり、冷媒回路を循環する冷媒量は増える。暖房モード時には、制御装置20は、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にする。第2、第3のレシーバ5b,5cに液冷媒が溜まり、冷媒回路を循環する冷媒量は減る。冷房モード時に循環する冷媒量は暖房モード時に循環する冷媒量よりも多くなる。   In the air conditioner shown in FIG. 2, when the volume of the outdoor heat exchanger 14 is larger than the volume of the indoor heat exchanger 13, in the cooling mode, the control device 20 controls the first flow rate adjusting device 6a, 2 Fully open the flow rate adjusting device 6b. Liquid refrigerant accumulates only in the first receiver 5a, and the amount of refrigerant circulating in the refrigerant circuit increases. In the heating mode, the control device 20 controls the first flow rate adjusting device 6a and fully opens the second flow rate adjusting device 6b. Liquid refrigerant accumulates in the second and third receivers 5b and 5c, and the amount of refrigerant circulating in the refrigerant circuit decreases. The amount of refrigerant circulating in the cooling mode is larger than the amount of refrigerant circulating in the heating mode.

室内熱交換器13の容積が室外熱交換器14の容積より大であるとき、冷房モード時には、制御装置20は、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にする。第1、第2レシーバ5a,5bに液冷媒が溜まり、冷媒回路を循環する冷媒量は減る。暖房モード時には、制御装置20は、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にする。第3のレシーバ5cだけに液冷媒が溜まり、冷媒回路を循環する冷媒量は増える。暖房モード時に循環する冷媒量は冷房モード時に循環する冷媒量よりも多くなる。   When the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14, in the cooling mode, the control device 20 controls the second flow rate adjustment device 6b to fully open the first flow rate adjustment device 6a. . Liquid refrigerant accumulates in the first and second receivers 5a and 5b, and the amount of refrigerant circulating in the refrigerant circuit decreases. In the heating mode, the control device 20 controls the second flow rate adjusting device 6b to fully open the first flow rate adjusting device 6a. Liquid refrigerant accumulates only in the third receiver 5c, and the amount of refrigerant circulating in the refrigerant circuit increases. The amount of refrigerant circulating in the heating mode is larger than the amount of refrigerant circulating in the cooling mode.

(第3の実施形態)
本実施形態の空気調和機では、図6に示すように、レシーバが第1、第2レシーバ5A,5Bとされ、第1レシーバ5Aの上流側に高圧側流量調整装置6Aが配され、第2レシーバ5Bの上流側に低圧側流量調整装置6Bが配される。低圧側流量調整装置6Bは第1レシーバ5Aと第2レシーバ5Bとの間に位置する。なお、レシーバ5を除くその他の構成および動作は、第1の実施形態と同じである。
(Third embodiment)
In the air conditioner of the present embodiment, as shown in FIG. 6, the receivers are first and second receivers 5A and 5B, the high-pressure flow rate adjustment device 6A is disposed upstream of the first receiver 5A, and the second A low pressure side flow rate adjusting device 6B is arranged upstream of the receiver 5B. The low pressure side flow rate adjusting device 6B is located between the first receiver 5A and the second receiver 5B. Other configurations and operations excluding the receiver 5 are the same as those in the first embodiment.

制御装置20が、高圧側流量調整装置6Aを制御し、低圧側流量調整装置6Bを全開にすると、第1、第2レシーバ5A,5Bには、冷媒が出入りしない。制御装置20が、低圧側流量調整装置6Bを制御し、高圧側流量調整装置6Aを全開にすると、第1レシーバ5Aに液冷媒が溜まる。   When the control device 20 controls the high pressure side flow rate adjustment device 6A and fully opens the low pressure side flow rate adjustment device 6B, the refrigerant does not enter and exit the first and second receivers 5A and 5B. When the control device 20 controls the low pressure side flow rate adjustment device 6B and fully opens the high pressure side flow rate adjustment device 6A, the liquid refrigerant accumulates in the first receiver 5A.

このように、レシーバ5の下流側に位置する流量調整装置6が動作すると、この流量調整装置6の上流に位置するレシーバ5に液冷媒が溜まる。すなわち、下流側の流量調整装置6が動作したときにレシーバ5に溜まる冷媒量は、上流側の流量調整装置6が動作したときにレシーバ5に溜まる冷媒量よりも多くなる。そのため、高圧側流量調整装置6Aを制御したときに循環する冷媒量は、低圧側流量調整装置6Bを制御したときに循環する冷媒量よりも多くなる。したがって、動作させる流量調整装置6に応じて冷媒回路を循環する冷媒量を調整することが可能となり、運転状況に応じた最適な冷媒量にすることができる。   As described above, when the flow rate adjusting device 6 positioned on the downstream side of the receiver 5 is operated, the liquid refrigerant is accumulated in the receiver 5 positioned on the upstream side of the flow rate adjusting device 6. That is, the amount of refrigerant that accumulates in the receiver 5 when the downstream flow rate adjustment device 6 operates is greater than the amount of refrigerant that accumulates in the receiver 5 when the upstream flow rate adjustment device 6 operates. Therefore, the amount of refrigerant that circulates when the high-pressure flow rate adjustment device 6A is controlled is larger than the amount of refrigerant that circulates when the low-pressure flow rate adjustment device 6B is controlled. Therefore, it is possible to adjust the amount of refrigerant circulating in the refrigerant circuit according to the flow rate adjusting device 6 to be operated, and it is possible to set the optimum amount of refrigerant according to the operation state.

ここで、室外熱交換器14の容積と室内熱交換器13の容積とが異なる場合、運転モードによって最適な冷媒量は異なる。室外熱交換器14の容積が室内熱交換器13の容積より大の場合、冷房モード時の最適な冷媒量は暖房モード時の最適な冷媒量よりも多い。そのため、図7に示すように、第1レシーバ5aが室外熱交換器14側に配され、第2レシーバ5bが室内熱交換器13側に配される。第1流量調整装置6aは、第1レシーバ5aと室外熱交換器14との間に配され、第2流量調整装置6bは、第1レシーバ5aと第2レシーバ5bとの間に配される。   Here, when the volume of the outdoor heat exchanger 14 and the volume of the indoor heat exchanger 13 are different, the optimum refrigerant amount differs depending on the operation mode. When the volume of the outdoor heat exchanger 14 is larger than the volume of the indoor heat exchanger 13, the optimum refrigerant amount in the cooling mode is larger than the optimum refrigerant amount in the heating mode. Therefore, as shown in FIG. 7, the first receiver 5a is arranged on the outdoor heat exchanger 14 side, and the second receiver 5b is arranged on the indoor heat exchanger 13 side. The first flow rate adjusting device 6a is arranged between the first receiver 5a and the outdoor heat exchanger 14, and the second flow rate adjusting device 6b is arranged between the first receiver 5a and the second receiver 5b.

冷房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第1、第2レシーバ5a,5bでは、冷媒は出入りしない。循環する冷媒量は大となる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第1レシーバ5aに液冷媒が溜まり、第2レシーバ5bには、冷媒は溜まらない。循環する冷媒量は中となる。   When the control device 20 controls the first flow rate adjustment device 6a and fully opens the second flow rate adjustment device 6b in the cooling mode, the refrigerant does not enter and exit the first and second receivers 5a and 5b. The amount of circulating refrigerant becomes large. When the control device 20 controls the second flow rate adjusting device 6b and fully opens the first flow rate adjusting device 6a, the liquid refrigerant is accumulated in the first receiver 5a, and no refrigerant is accumulated in the second receiver 5b. The amount of circulating refrigerant is medium.

暖房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第1、第2レシーバ5a,5bに液冷媒が溜まる。循環する冷媒量は小となる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第2レシーバ5bに液冷媒が溜まり、第1レシーバ5aには、冷媒は溜まらない。循環する冷媒量は中となる。したがって、冷房モード時に循環する冷媒量を暖房モード時に循環する冷媒量よりも多くすることができる。   When the control device 20 controls the first flow rate adjustment device 6a and fully opens the second flow rate adjustment device 6b in the heating mode, liquid refrigerant accumulates in the first and second receivers 5a and 5b. The amount of circulating refrigerant is small. When the control device 20 controls the second flow rate adjusting device 6b and fully opens the first flow rate adjusting device 6a, the liquid refrigerant is accumulated in the second receiver 5b, and no refrigerant is accumulated in the first receiver 5a. The amount of circulating refrigerant is medium. Therefore, the amount of refrigerant circulating in the cooling mode can be made larger than the amount of refrigerant circulating in the heating mode.

室内熱交換器13の容積が室外熱交換器14の容積より大の場合、暖房モード時の最適な冷媒量は冷房モード時の最適な冷媒量よりも多い。そのため、図8に示すように、第1レシーバ5aが室外熱交換器側に配され、第2レシーバ5bが室内熱交換器側に配される。第1流量調整装置6aは、第1レシーバ5aと第2レシーバ5bとの間に配され、第2流量調整装置6bは、第1レシーバ5aと室内熱交換器13との間に配される。   When the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14, the optimum refrigerant amount in the heating mode is larger than the optimum refrigerant amount in the cooling mode. Therefore, as shown in FIG. 8, the 1st receiver 5a is distribute | arranged to the outdoor heat exchanger side, and the 2nd receiver 5b is distribute | arranged to the indoor heat exchanger side. The first flow rate adjusting device 6a is arranged between the first receiver 5a and the second receiver 5b, and the second flow rate adjusting device 6b is arranged between the first receiver 5a and the indoor heat exchanger 13.

冷房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第1レシーバ5aに液冷媒が溜まり、第2レシーバ5bには、冷媒は溜まらない。循環する冷媒量は中となる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第1、第2レシーバ5a,5bに液冷媒が溜まる。循環する冷媒量は小となる。   In the cooling mode, when the control device 20 controls the first flow rate adjusting device 6a and fully opens the second flow rate adjusting device 6b, liquid refrigerant accumulates in the first receiver 5a, and no refrigerant accumulates in the second receiver 5b. Absent. The amount of circulating refrigerant is medium. When the control device 20 controls the second flow rate adjustment device 6b and fully opens the first flow rate adjustment device 6a, liquid refrigerant accumulates in the first and second receivers 5a and 5b. The amount of circulating refrigerant is small.

暖房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第2レシーバ5bに液冷媒が溜まり、第1レシーバ5aには、冷媒は溜まらない。循環する冷媒量は中となる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第1、第2レシーバ5a,5bには、冷媒は溜まらない。循環する冷媒量は大となる。したがって、暖房モード時に循環する冷媒量を冷房モード時に循環する冷媒量よりも多くすることができる。   In the heating mode, when the control device 20 controls the first flow rate adjusting device 6a and fully opens the second flow rate adjusting device 6b, liquid refrigerant accumulates in the second receiver 5b, and no refrigerant accumulates in the first receiver 5a. Absent. The amount of circulating refrigerant is medium. When the control device 20 controls the second flow rate adjusting device 6b and fully opens the first flow rate adjusting device 6a, no refrigerant accumulates in the first and second receivers 5a and 5b. The amount of circulating refrigerant becomes large. Therefore, the amount of refrigerant circulating in the heating mode can be made larger than the amount of refrigerant circulating in the cooling mode.

(第4の実施形態)
上記の各実施形態では、複数のレシーバ5の容積は同じであるが、本実施形態では、各レシーバ5の容積がそれぞれ異なる。図1に示す3つのレシーバ5において、第1レシーバ5Aの容積がA、第2レシーバ5Bの容積がB、第3レシーバ5Cの容積がCとされる。A、B、Cはそれぞれ異なる値である。なお、その他の構成および動作は第1の実施形態と同じである。
(Fourth embodiment)
In the above embodiments, the volumes of the plurality of receivers 5 are the same, but in the present embodiment, the volumes of the receivers 5 are different. In the three receivers 5 shown in FIG. 1, the volume of the first receiver 5A is A, the volume of the second receiver 5B is B, and the volume of the third receiver 5C is C. A, B, and C are different values. Other configurations and operations are the same as those in the first embodiment.

制御装置20が、高圧側流量調整装置6aを制御し、低圧側流量調整装置6bを全開にすると、第1レシーバ5Aに液冷媒が溜まり、第2、第3レシーバ5B,5Cには、冷媒は溜まらない。レシーバ5に溜まる冷媒量は最大Aとなる。制御装置20が、低圧側流量調整装置6Bを制御し、高圧側流量調整装置6Aを全開にすると、第1、第2レシーバ5A,5Bに液冷媒が溜まり、第3レシーバ5Cには、冷媒は溜まらない。レシーバ5に溜まる冷媒量は最大A+Bとなる。   When the control device 20 controls the high pressure side flow rate adjustment device 6a and fully opens the low pressure side flow rate adjustment device 6b, the liquid refrigerant is accumulated in the first receiver 5A, and the second and third receivers 5B and 5C have no refrigerant. I do not collect. The maximum amount of refrigerant accumulated in the receiver 5 is A. When the control device 20 controls the low pressure side flow rate adjustment device 6B and fully opens the high pressure side flow rate adjustment device 6A, liquid refrigerant is accumulated in the first and second receivers 5A and 5B, and the refrigerant is stored in the third receiver 5C. I do not collect. The maximum amount of refrigerant accumulated in the receiver 5 is A + B.

このように、各流量調整装置6を制御することにより、各レシーバ5の容積に応じて循環する冷媒量が異なる。したがって、動作させる流量調整装置6に応じて冷媒回路を循環する冷媒量を細かく調整することが可能となり、運転状況に応じた最適な冷媒量にすることができる。   In this way, by controlling each flow rate adjusting device 6, the amount of refrigerant circulating varies depending on the volume of each receiver 5. Therefore, the amount of refrigerant circulating in the refrigerant circuit can be finely adjusted according to the flow rate adjusting device 6 to be operated, and the optimum amount of refrigerant according to the operating condition can be obtained.

図2に示す3つのレシーバ5では、第1レシーバ5aの容積がA、第2レシーバ5bの容積がB、第3レシーバ5cの容積がCとされる。冷房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第1レシーバ5aに液冷媒が溜まる。レシーバ5に溜まる冷媒量は最大Aとなる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第1、第2レシーバ5a,5bに液冷媒が溜まる。レシーバ5に溜まる冷媒量は最大A+Bとなる。   In the three receivers 5 shown in FIG. 2, the volume of the first receiver 5a is A, the volume of the second receiver 5b is B, and the volume of the third receiver 5c is C. In the cooling mode, when the control device 20 controls the first flow rate adjusting device 6a and fully opens the second flow rate adjusting device 6b, liquid refrigerant accumulates in the first receiver 5a. The maximum amount of refrigerant accumulated in the receiver 5 is A. When the control device 20 controls the second flow rate adjustment device 6b and fully opens the first flow rate adjustment device 6a, liquid refrigerant accumulates in the first and second receivers 5a and 5b. The maximum amount of refrigerant accumulated in the receiver 5 is A + B.

暖房モード時に、制御装置20が、第1流量調整装置6aを制御し、第2流量調整装置6bを全開にすると、第2、第3レシーバ5b,5cに液冷媒が溜まる。レシーバ5に溜まる冷媒量は最大B+Cとなる。制御装置20が、第2流量調整装置6bを制御し、第1流量調整装置6aを全開にすると、第3レシーバ5cに液冷媒が溜まる。レシーバ5に溜まる冷媒量は最大Cとなる。   When the control device 20 controls the first flow rate adjusting device 6a and fully opens the second flow rate adjusting device 6b in the heating mode, liquid refrigerant accumulates in the second and third receivers 5b and 5c. The maximum amount of refrigerant accumulated in the receiver 5 is B + C. When the control device 20 controls the second flow rate adjusting device 6b and fully opens the first flow rate adjusting device 6a, liquid refrigerant accumulates in the third receiver 5c. The maximum amount of refrigerant accumulated in the receiver 5 is C.

このように、複数のレシーバ5の容積が異なっていると、運転モードに応じて冷媒回路を循環する冷媒量を細かく調整することが可能となる。したがって、各流量調整装置6を制御することにより、運転状況に応じて容易に最適な冷媒量にすることができる。   Thus, when the volumes of the plurality of receivers 5 are different, it is possible to finely adjust the amount of refrigerant circulating in the refrigerant circuit according to the operation mode. Therefore, by controlling each flow rate adjusting device 6, it is possible to easily obtain the optimum refrigerant amount according to the operation state.

(第5の実施形態)
空調運転の起動時、冷媒回路を循環する冷媒量が多いと、冷凍サイクルが効率よく安定する。そこで、本実施形態では、容積の異なるレシーバ5の並び順として、冷媒の流れ方向の上流側に位置するレシーバ5の容積を下流側に位置する他のレシーバ5の容積よりも小とする。なお、その他の構成および動作は第1の実施形態と同じである。
(Fifth embodiment)
If the amount of refrigerant circulating through the refrigerant circuit is large at the start of the air conditioning operation, the refrigeration cycle is efficiently stabilized. Therefore, in the present embodiment, as the arrangement order of the receivers 5 having different volumes, the volume of the receiver 5 positioned on the upstream side in the refrigerant flow direction is set smaller than the volume of the other receivers 5 positioned on the downstream side. Other configurations and operations are the same as those in the first embodiment.

すなわち、凝縮器2と蒸発器4との間に配された複数のレシーバ5のうち、凝縮器2に近い位置にあるレシーバ5の容積が最小とされ、蒸発器4に近い位置にあるレシーバ5の容積が最大とされる。例えば、図1に示すように、レシーバ5が3つある場合、上流側の第1レシーバ5Aの容積は小、第2レシーバ5Bの容積は中、下流側の第3レシーバ5Cの容積は大となる。   That is, among the plurality of receivers 5 arranged between the condenser 2 and the evaporator 4, the volume of the receiver 5 at a position close to the condenser 2 is minimized, and the receiver 5 at a position close to the evaporator 4. The volume of is maximized. For example, as shown in FIG. 1, when there are three receivers 5, the volume of the first receiver 5A on the upstream side is small, the volume of the second receiver 5B is medium, and the volume of the third receiver 5C on the downstream side is large. Become.

高圧側流量調整装置6Aが制御され、低圧側流量調整装置6Bが全開にされたとき、第1レシーバ5Aに冷媒が溜まる。低圧側流量調整装置6Bが制御され、高圧側流量調整装置6Aが全開にされたとき、第1、第2レシーバ5A,5Bに冷媒が溜まる。いずれの場合でも、下流側のレシーバ5には、冷媒は溜まらない。冷媒が溜まるレシーバ5は小、中の容積を有するレシーバ5となるため、全レシーバ5に溜められる冷媒量は容積が大のレシーバ5に溜まる場合に比べて少なく、冷媒回路を循環する冷媒量が多くなる。   When the high pressure side flow rate adjustment device 6A is controlled and the low pressure side flow rate adjustment device 6B is fully opened, the refrigerant accumulates in the first receiver 5A. When the low pressure side flow rate adjusting device 6B is controlled and the high pressure side flow rate adjusting device 6A is fully opened, the refrigerant accumulates in the first and second receivers 5A and 5B. In any case, the refrigerant does not accumulate in the downstream receiver 5. Since the receiver 5 in which the refrigerant is stored becomes a receiver 5 having a small and medium volume, the amount of refrigerant stored in all the receivers 5 is smaller than that in the receiver 5 having a large volume, and the amount of refrigerant circulating in the refrigerant circuit is small. Become more.

ここで、凝縮器2に近い位置では、循環する冷媒の圧力が高いので、レシーバ5に冷媒が溜まりやすい。しかし、循環する冷媒量を多くする場合、レシーバ5の容積が大きいと、冷媒が多く溜まってしまう。冷媒が溜まり過ぎるのを避けるため、高圧側にあるレシーバ5の容積は小さいほうがよい。したがって、容積の小さいレシーバ5を凝縮器2に近い位置に設けることは、循環する冷媒量を多くするときに好適な配置となる。   Here, at a position close to the condenser 2, since the pressure of the circulating refrigerant is high, the refrigerant tends to accumulate in the receiver 5. However, when increasing the amount of circulating refrigerant, if the volume of the receiver 5 is large, a large amount of refrigerant accumulates. The volume of the receiver 5 on the high pressure side should be small in order to avoid excessive accumulation of refrigerant. Therefore, providing the receiver 5 with a small volume at a position close to the condenser 2 is a suitable arrangement when increasing the amount of refrigerant to be circulated.

また、冷媒回路を循環する最適な冷媒量は運転状況に応じて異なる。複数のレシーバ5が容積の小さいものから順に配置されているとき、制御する流量調整装置6に応じて全レシーバ5に溜まる冷媒量を容易に計算できる。したがって、循環する冷媒量を最適にするための各流量調整装置6の制御を容易に行える。   Further, the optimum amount of refrigerant circulating through the refrigerant circuit varies depending on the operating conditions. When the plurality of receivers 5 are arranged in order from the one with the smallest volume, the amount of refrigerant accumulated in all the receivers 5 can be easily calculated according to the flow rate adjusting device 6 to be controlled. Therefore, it is possible to easily control each flow rate adjusting device 6 for optimizing the circulating refrigerant amount.

ところで、室内外の熱交換器13,14の容積は設置時に決まっている。それぞれの熱交換器13,14の容積に基づいて、循環する冷媒量が冷房モード時に多く必要か暖房モード時に多く必要かが決まる。これに基づいて、容積の異なるレシーバ5の並び順が決められる。   By the way, the volume of the indoor and outdoor heat exchangers 13 and 14 is determined at the time of installation. Based on the volume of each of the heat exchangers 13 and 14, it is determined whether a large amount of circulating refrigerant is necessary in the cooling mode or in the heating mode. Based on this, the arrangement order of the receivers 5 having different volumes is determined.

室外熱交換器14の容積が室内熱交換器13の容積より大のとき、冷房モード時に必要な冷媒量は暖房モード時よりも多い。このとき、図2に示す3つのレシーバ5において、第1レシーバ5aの容積は小、第2レシーバ5bの容積は中、第3レシーバ5cの容積は大とされる。   When the volume of the outdoor heat exchanger 14 is larger than the volume of the indoor heat exchanger 13, the amount of refrigerant required in the cooling mode is larger than that in the heating mode. At this time, in the three receivers 5 shown in FIG. 2, the volume of the first receiver 5a is small, the volume of the second receiver 5b is medium, and the volume of the third receiver 5c is large.

冷房モード時に、第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第1レシーバ5aに液冷媒が溜まる。第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第1、第2レシーバ5a,5bに液冷媒が溜まる。いずれの場合でも、第3レシーバ5cには、冷媒は溜まらない。   In the cooling mode, when the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, liquid refrigerant accumulates in the first receiver 5a. When the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, liquid refrigerant accumulates in the first and second receivers 5a and 5b. In any case, no refrigerant accumulates in the third receiver 5c.

暖房モード時に、第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第2、第3レシーバ5b,5cに液冷媒が溜まる。第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第3レシーバ5cに液冷媒が溜まる。   In the heating mode, when the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, liquid refrigerant accumulates in the second and third receivers 5b and 5c. When the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, liquid refrigerant accumulates in the third receiver 5c.

冷房モード時には、小、中の容積を有するレシーバ5に液冷媒が溜り、暖房モード時には、中、大の容積を有するレシーバ5に液冷媒が溜まる。そのため、レシーバ5に溜められる冷媒量は暖房モード時に多く、冷房モード時には少なくなり、冷房モード時に冷媒回路を循環する冷媒量が暖房モード時より多くなる。   In the cooling mode, liquid refrigerant accumulates in the receiver 5 having a small and medium volume, and in the heating mode, liquid refrigerant accumulates in the receiver 5 having a medium and large volume. Therefore, the amount of refrigerant stored in the receiver 5 is large during the heating mode, decreases during the cooling mode, and the amount of refrigerant circulating in the refrigerant circuit during the cooling mode is greater than during the heating mode.

室内熱交換器13の容積が室外熱交換器14の容積より大のとき、暖房モード時に必要な冷媒量は冷房モード時よりも多い。このとき、図2に示す3つのレシーバ5において、第3レシーバ5cの容積は小、第2レシーバ5bの容積は中、第1レシーバ5aの容積は大とされる。   When the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14, the amount of refrigerant required in the heating mode is larger than that in the cooling mode. At this time, in the three receivers 5 shown in FIG. 2, the volume of the third receiver 5c is small, the volume of the second receiver 5b is medium, and the volume of the first receiver 5a is large.

暖房モード時に、第2流量調整装置6bが制御され、第1流量調整装置5aが全開にされたとき、第3レシーバ5cに液冷媒が溜まる。第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第2、第3レシーバ5b,5cに液冷媒が溜まる。   In the heating mode, when the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 5a is fully opened, the liquid refrigerant is accumulated in the third receiver 5c. When the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, liquid refrigerant accumulates in the second and third receivers 5b and 5c.

冷房モード時に、第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第1レシーバ5aに液冷媒が溜まる。第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第1、第2レシーバ5a,5bに液冷媒が溜まる。   In the cooling mode, when the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, liquid refrigerant accumulates in the first receiver 5a. When the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, liquid refrigerant accumulates in the first and second receivers 5a and 5b.

暖房モード時には、小、中の容積を有するレシーバ5に液冷媒が溜り、冷房モード時には、中、大の容積を有するレシーバ5に液冷媒が溜まる。そのため、レシーバ5に溜められる冷媒量は冷房モード時に多く、暖房モード時には少なくなり、暖房モード時に冷媒回路を循環する冷媒量が冷房モード時より多くなる。   In the heating mode, liquid refrigerant accumulates in the receiver 5 having a small and medium volume, and in the cooling mode, liquid refrigerant accumulates in the receiver 5 having a medium and large volume. Therefore, the amount of refrigerant stored in the receiver 5 is large in the cooling mode, decreases in the heating mode, and the amount of refrigerant circulating in the refrigerant circuit in the heating mode is larger than in the cooling mode.

また、レシーバ5が2つの場合、室外熱交換器14の容積が室内熱交換器13の容積より大のとき、図7に示す第1レシーバ5aの容積が小、第2レシーバ5bの容積が大とされる。冷房モード時に、第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第1レシーバ5aに液冷媒が溜まる。第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、各レシーバ5a,5bには、冷媒は溜まらない。   When the number of the receivers 5 is two and the volume of the outdoor heat exchanger 14 is larger than the volume of the indoor heat exchanger 13, the volume of the first receiver 5a shown in FIG. 7 is small and the volume of the second receiver 5b is large. It is said. In the cooling mode, when the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, liquid refrigerant is accumulated in the first receiver 5a. When the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, no refrigerant accumulates in each receiver 5a, 5b.

暖房モード時に、第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第2レシーバ5bに液冷媒が溜まる。第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第1、第2レシーバ5a,5bに液冷媒が溜まる。この場合でも、冷房モード時に冷媒回路を循環する冷媒量が暖房モード時よりも多くなる。   In the heating mode, when the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, the liquid refrigerant is accumulated in the second receiver 5b. When the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, liquid refrigerant accumulates in the first and second receivers 5a and 5b. Even in this case, the amount of refrigerant circulating in the refrigerant circuit in the cooling mode is larger than that in the heating mode.

室内熱交換器13の容積が室外熱交換器14の容積より大のとき、図8に示す第2レシーバ5bの容積が小、第1レシーバ5aの容積が大とされる。冷房モード時に、第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第2レシーバ5bに液冷媒が溜まる。第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、第1、第2レシーバ5a,5bに液冷媒が溜まる。   When the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14, the volume of the second receiver 5b shown in FIG. 8 is small and the volume of the first receiver 5a is large. In the cooling mode, when the first flow rate adjusting device 6a is controlled and the second flow rate adjusting device 6b is fully opened, the liquid refrigerant is accumulated in the second receiver 5b. When the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, liquid refrigerant accumulates in the first and second receivers 5a and 5b.

暖房モード時に、第2流量調整装置6bが制御され、第1流量調整装置6aが全開にされたとき、各レシーバ5a,5bには、冷媒は溜まらない。第1流量調整装置6aが制御され、第2流量調整装置6bが全開にされたとき、第2レシーバ5bに液冷媒が溜まる。この場合でも、暖房モード時に冷媒回路を循環する冷媒量が冷房モード時よりも多くなる。   In the heating mode, when the second flow rate adjusting device 6b is controlled and the first flow rate adjusting device 6a is fully opened, no refrigerant is accumulated in the receivers 5a and 5b. When the first flow control device 6a is controlled and the second flow control device 6b is fully opened, the liquid refrigerant is accumulated in the second receiver 5b. Even in this case, the amount of refrigerant circulating in the refrigerant circuit in the heating mode is larger than that in the cooling mode.

(第6の実施形態)
空調運転中、流量調整装置は過熱度の変化等の運転状況に応じて制御される。流量調整装置6の制御に応じて、レシーバ5に溜まる冷媒量が変動し、冷媒回路を循環する冷媒が調整される。流量調整装置6が全開されると、流量調整装置6を通過する冷媒量が多くなる。
(Sixth embodiment)
During the air conditioning operation, the flow rate adjusting device is controlled in accordance with an operation state such as a change in superheat degree. According to the control of the flow rate adjusting device 6, the amount of refrigerant accumulated in the receiver 5 varies, and the refrigerant circulating in the refrigerant circuit is adjusted. When the flow control device 6 is fully opened, the amount of refrigerant passing through the flow control device 6 increases.

ところで、冷媒が流量調整装置6を通過するときに圧力損失が生じる。流量調整装置6が多くなるほど、圧力損失も大きくなる。圧力損失が大きくなると、冷媒が蒸発器4に流れ込みにくくなり、過熱度が大きくなる。そのため、圧縮機1からの吐出温度が上昇し、空調能力が不足して、運転効率が悪くなる。流量調整装置6の開度を大きくすることにより、蒸発器4に流れ込む冷媒を増やすことができる。   By the way, pressure loss occurs when the refrigerant passes through the flow control device 6. As the flow rate adjusting device 6 increases, the pressure loss also increases. When the pressure loss increases, the refrigerant hardly flows into the evaporator 4 and the degree of superheat increases. Therefore, the discharge temperature from the compressor 1 rises, the air conditioning capability is insufficient, and the operation efficiency is deteriorated. The refrigerant flowing into the evaporator 4 can be increased by increasing the opening degree of the flow rate adjusting device 6.

しかし、流量調整装置6が全開あるいは全開近くの開度であるとき、循環する冷媒量が不足するような事態が起こった場合、これ以上流量調整装置6を開いても、循環する冷媒量を増やすことができない。すなわち、流量調整装置6の制御により対処することができない。   However, when the flow control device 6 is fully open or close to full open, if a situation occurs in which the amount of circulating refrigerant is insufficient, the amount of circulating refrigerant is increased even if the flow control device 6 is opened further. I can't. That is, it cannot be dealt with by the control of the flow rate adjusting device 6.

本実施形態では、このような場合に、圧縮機1の回転数を下げる制御を行うことにより、流量調整装置6を制御可能にして、冷媒量を調整できるようにする。すなわち、複数の流量調整装置6の開度が所定の開度以上になったとき、制御装置20は、圧縮機1の回転数を下げる。   In this embodiment, in such a case, the flow rate adjusting device 6 is made controllable by adjusting the rotation speed of the compressor 1 so that the refrigerant amount can be adjusted. That is, when the opening degree of the plurality of flow rate adjusting devices 6 becomes equal to or larger than the predetermined opening degree, the control device 20 decreases the rotational speed of the compressor 1.

図9に示すように、冷媒回路の室外熱交換器14と室内熱交換器13との間に2つの流量調整装置6a,6bが設けられ、第1流量調整装置6aと第2流量調整装置6bとの間に1つのレシーバ5が設けられる。なお、レシーバ5が1つであることを除いて、その他の構成および動作は上記の各実施形態と同じである。   As shown in FIG. 9, two flow control devices 6a and 6b are provided between the outdoor heat exchanger 14 and the indoor heat exchanger 13 of the refrigerant circuit, and the first flow control device 6a and the second flow control device 6b. Between the two, one receiver 5 is provided. The other configurations and operations are the same as those in the above embodiments except that there is one receiver 5.

空調運転が行われると、制御装置20は、冷凍サイクルが安定したことを確認してから各流量調整装置6を制御する。例えば冷房モード時には、第2流量調整装置6bが全開にされ、第1流量調整装置6aの開度が設定された開度にされる。そして、運転状況に応じて第1流量調整装置6aが制御される。過熱度が大きくなると、制御装置20は、第1流量調整装置6aの開度が大きくなるように第1流量調整装置6aを制御する。第1流量調整装置6aを通る冷媒量が多くなり、室内熱交換器13に流れ込む冷媒が増え、過熱度が小さくなる。   When the air conditioning operation is performed, the control device 20 controls each flow rate adjusting device 6 after confirming that the refrigeration cycle is stable. For example, in the cooling mode, the second flow rate adjusting device 6b is fully opened, and the opening degree of the first flow rate adjusting device 6a is set to the set opening degree. And the 1st flow regulating device 6a is controlled according to an operation situation. When the degree of superheat increases, the control device 20 controls the first flow rate adjusting device 6a so that the opening degree of the first flow rate adjusting device 6a increases. The amount of refrigerant passing through the first flow rate adjusting device 6a increases, the amount of refrigerant flowing into the indoor heat exchanger 13 increases, and the degree of superheat decreases.

空調運転中、制御装置20は、循環する冷媒量を調整するために過熱度などの運転状況に応じて流量調整装置6の開度を変化させるが、流量調整装置6の制御により冷媒量を調整可能か否かを判断する。   During the air-conditioning operation, the control device 20 changes the opening degree of the flow rate adjusting device 6 according to the operating condition such as the degree of superheat in order to adjust the circulating refrigerant amount, but the refrigerant amount is adjusted by the control of the flow rate adjusting device 6. Determine if it is possible.

すなわち、図10に示すように、制御装置20は、第1、第2流量調整装置6a,6bの開度が所定の開度以上であるかをチェックする(S1)。所定の開度は、全開に近い開度とされ、例えば80%に設定される。なお、第2流量調整装置6bは全開にされるが、第2流量調整装置6bの開度は所定の開度以上であればよい。第1流量調整装置6aの開度が所定の開度以上になると、制御装置20は、流量調整装置6の制御により冷媒量を調整するのが不可能であると判断し、圧縮機1の回転数を下げるように圧縮機1を制御する(S2)。例えば、圧縮機1の回転数は500rpm下げられる。   That is, as shown in FIG. 10, the control device 20 checks whether the opening degree of the first and second flow rate adjusting devices 6a and 6b is equal to or larger than a predetermined opening degree (S1). The predetermined opening is an opening close to full opening, and is set to 80%, for example. In addition, although the 2nd flow volume adjustment apparatus 6b is fully opened, the opening degree of the 2nd flow volume adjustment apparatus 6b should just be more than a predetermined opening degree. When the opening degree of the first flow rate adjusting device 6a becomes equal to or larger than the predetermined opening degree, the control device 20 determines that it is impossible to adjust the refrigerant amount under the control of the flow rate adjusting device 6, and the rotation of the compressor 1 The compressor 1 is controlled so as to decrease the number (S2). For example, the rotation speed of the compressor 1 is reduced by 500 rpm.

圧縮機1の回転数が下がると、圧縮機1の回転数に応じた最適な冷媒量は少なくなる。そこで、制御装置20は、圧縮機1の回転数に応じて第1流量調整装置6aの開度を変更する(S3)。第1流量調整装置6aの開度は、低下した回転数に応じた開度となり、第1流量調整装置6aの開度は小さくなる。制御装置20は、変更後の開度が所定の開度以上であるかをチェックする(S2)。所定の開度以上である場合、制御装置20は、再度圧縮機1を制御して、圧縮機1の回転数を例えば500rpm下げる。圧縮機1の回転数の低下に応じて、第1流量調整装置6aの開度が小さくなるように変更される。   When the rotation speed of the compressor 1 decreases, the optimum refrigerant amount corresponding to the rotation speed of the compressor 1 decreases. Therefore, the control device 20 changes the opening degree of the first flow rate adjusting device 6a according to the rotational speed of the compressor 1 (S3). The opening degree of the first flow rate adjusting device 6a becomes an opening degree corresponding to the reduced rotational speed, and the opening degree of the first flow rate adjusting device 6a becomes small. The control device 20 checks whether the changed opening is equal to or greater than a predetermined opening (S2). When the opening degree is equal to or greater than the predetermined opening degree, the control device 20 controls the compressor 1 again to lower the rotational speed of the compressor 1 by, for example, 500 rpm. As the rotational speed of the compressor 1 decreases, the opening of the first flow rate adjusting device 6a is changed to be smaller.

第1流量調整装置6aの開度が所定の開度より小さくなると、図11に示すように、一定時間経過してから、制御装置20は、室温が設定温度よりも高くなったかをチェックする(S4)。室温が設定温度より高いとき、制御装置20は、圧縮機1の回転数を上げるように圧縮機1を制御する(S5)。例えば、圧縮機1の回転数は500rpm上げられる。制御装置20は、圧縮機1の回転数に応じて第1流量調整装置6aの開度を変更する(S6)。第1流量調整装置6aの開度は、圧縮機1の上昇した回転数に応じた開度となり、第1流量調整装置6aの開度は大きくなる。その後、制御装置20は、第1、第2流量調整装置6a,6bの開度が所定の開度以上であるかをチェックする(S1)。   When the opening degree of the first flow rate adjusting device 6a becomes smaller than the predetermined opening degree, as shown in FIG. 11, the controller 20 checks whether or not the room temperature has become higher than the set temperature after a certain time has passed ( S4). When the room temperature is higher than the set temperature, the control device 20 controls the compressor 1 so as to increase the rotational speed of the compressor 1 (S5). For example, the rotation speed of the compressor 1 is increased by 500 rpm. The control apparatus 20 changes the opening degree of the 1st flow volume adjustment apparatus 6a according to the rotation speed of the compressor 1 (S6). The opening degree of the first flow rate adjusting device 6a is an opening degree corresponding to the increased rotational speed of the compressor 1, and the opening degree of the first flow rate adjusting device 6a is increased. Thereafter, the control device 20 checks whether the opening degree of the first and second flow rate adjusting devices 6a and 6b is equal to or larger than a predetermined opening degree (S1).

空調負荷が大きい場合に、各流量調整装置6が全開あるいは全開近くになってこれ以上制御できない事態になっても、圧縮機1の回転数を下げることにより、圧縮機1の回転数に応じた最適な冷媒量は少なくなる。これに伴い流量調整装置6では、低下した回転数に応じた開度となり、第1流量調整装置6aの開度は小さくなるので、流量調整装置6の制御が可能となる。すなわち、過熱度が大きくなったとき、上記の制御によって流量調整装置6の開度を大きくすることができる。流量調整装置6の開度に変更によって、レシーバ5に溜まっている液冷媒が冷媒回路に排出されて、循環する冷媒量が多くなり、過熱度を小さくすることができる。したがって、流量調整装置6の制御により最適な冷媒量に調整することができる。   When the air conditioning load is large, even if each flow rate adjusting device 6 becomes fully open or close to full open and cannot be controlled any more, the number of rotations of the compressor 1 is decreased, so that the number of rotations of the compressor 1 is reduced. The optimum amount of refrigerant is reduced. Accordingly, the flow rate adjusting device 6 has an opening degree corresponding to the reduced rotational speed, and the opening amount of the first flow rate adjusting device 6a becomes small, so that the flow rate adjusting device 6 can be controlled. That is, when the degree of superheat increases, the opening degree of the flow rate adjusting device 6 can be increased by the above control. By changing to the opening degree of the flow rate adjusting device 6, the liquid refrigerant accumulated in the receiver 5 is discharged to the refrigerant circuit, and the amount of circulating refrigerant increases and the degree of superheat can be reduced. Therefore, it can be adjusted to the optimum refrigerant amount by the control of the flow rate adjusting device 6.

空調負荷が小さい場合、上記の制御を行うことにより、循環する冷媒量を少なくしても十分な空調負荷を得ることができる。そのため、圧縮機1の回転数を低くすることができ、空気調和機の省電力化を図れる。空調負荷が大きい場合、上記の制御を行うことにより、循環する冷媒量を多くでき、適正な過熱度を維持することができる。そのため、空調能力が高く、かつ効率のよい空調運転を行える。   When the air conditioning load is small, a sufficient air conditioning load can be obtained by performing the above control even if the amount of circulating refrigerant is reduced. Therefore, the rotation speed of the compressor 1 can be lowered, and power saving of the air conditioner can be achieved. When the air conditioning load is large, the amount of refrigerant circulating can be increased by performing the above control, and an appropriate degree of superheat can be maintained. For this reason, air conditioning capability is high and efficient air conditioning operation can be performed.

また、特に高湿度で外気温が高いといった特定の環境のとき、空調負荷が大きくなるので、循環する冷媒量を多くしなければならない。しかし、流量調整装置6を全開にしても、冷媒が流量調整装置6を通る際の圧力損失により蒸発器4に流れ込む冷媒が足らなくなり、蒸発器4に温度むらが発生する。室温とほぼ同じ温度のガス冷媒が蒸発器4である室内熱交換器13に流れ込むと、吸い込まれた室内の空気に含まれる水分が室内熱交換器13で十分に凝縮せずに吹出口に流れ、この空気が吹出口を通るときに吹出口の壁に露が付く。溜まった露が吹き出される風によって飛ばされ、吹出口から水が室内に飛散する。   Also, especially in a specific environment where the humidity is high and the outside air temperature is high, the air conditioning load increases, so the amount of circulating refrigerant must be increased. However, even if the flow control device 6 is fully opened, the refrigerant flows into the evaporator 4 due to pressure loss when the refrigerant passes through the flow control device 6, and temperature unevenness occurs in the evaporator 4. When a gas refrigerant having substantially the same temperature as room temperature flows into the indoor heat exchanger 13 that is the evaporator 4, moisture contained in the sucked indoor air flows to the outlet without being sufficiently condensed in the indoor heat exchanger 13. When the air passes through the air outlet, dew is attached to the wall of the air outlet. The accumulated dew is blown out by the blown wind, and water is scattered from the outlet into the room.

このような特定環境において、空調負荷が大きいときに上記の制御を行うことにより、冷媒の循環量を調整して、流量調整装置6を全開近くまで開かなくても制御可能な範囲で動作させることができる。これにより、冷媒不足を解消できる。したがって、蒸発器4に温度むらが生じないので、露付きを防止でき、水の飛散を防ぐことができる。   In such a specific environment, by performing the above-described control when the air conditioning load is large, the circulation amount of the refrigerant is adjusted so that the flow rate adjusting device 6 can be operated within a controllable range without being almost fully opened. Can do. Thereby, the refrigerant shortage can be solved. Therefore, since the temperature unevenness does not occur in the evaporator 4, it is possible to prevent dew condensation and water scattering.

なお、暖房モードで空調運転が行われるときにも、上記の制御が行われる。空調負荷に応じて流量調整装置6を制御することができ、最適な冷媒量に調整することができる。また、流量調整装置6が複数あるとき、流量調整装置6が1つのときよりも圧力損失が大きくなるが、上記と同様の制御を行うことにより、冷媒量が不足することをなくすことができ、効率のよい空調運転を行える。   The above control is also performed when the air conditioning operation is performed in the heating mode. The flow rate adjusting device 6 can be controlled according to the air conditioning load, and can be adjusted to the optimum refrigerant amount. Further, when there are a plurality of flow rate adjusting devices 6, the pressure loss is larger than when there is one flow rate adjusting device 6, but by performing the same control as described above, it is possible to eliminate the shortage of the refrigerant amount, Efficient air conditioning operation can be performed.

また、レシーバ5が複数設けられ、各レシーバ5に応じて流量調整装置6も複数以上設けられている冷媒回路においても、全ての流量調整装置6が所定の開度以上になったとき、上記と同様の制御が行われる。   Also, in the refrigerant circuit in which a plurality of receivers 5 are provided and a plurality of flow rate adjusting devices 6 are provided in accordance with each receiver 5, when all the flow rate adjusting devices 6 have reached a predetermined opening degree or more, Similar control is performed.

(第7の実施形態)
上記のように、冷房モードで空調運転中、高湿度で外気温が高い特定の環境では、空調負荷が大きくなる。空調能力を高めるために循環する冷媒量を多くしなければならない。しかし、流量調整装置6を全開あるいは全開近くまでにしても、冷媒が流量調整装置6を通る際の圧力損失により、室内熱交換器13において冷媒不足が生じ、吹出口に露が付くといった問題が生じる。そこで、本実施形態では、このような露付きを防止するために、制御装置20は、露付き防止制御を行う。なお、その他の構成および動作は第6の実施形態と同じである。
(Seventh embodiment)
As described above, during the air conditioning operation in the cooling mode, the air conditioning load increases in a specific environment with high humidity and high outside air temperature. In order to increase the air conditioning capacity, the amount of circulating refrigerant must be increased. However, even when the flow rate adjusting device 6 is fully opened or close to full open, there is a problem that the refrigerant is insufficient in the indoor heat exchanger 13 due to pressure loss when the refrigerant passes through the flow rate adjusting device 6 and dew is attached to the outlet. Arise. Therefore, in the present embodiment, in order to prevent such dew, the control device 20 performs dew prevention control. Other configurations and operations are the same as those in the sixth embodiment.

冷房モードで空調運転が行われているとき、制御装置20は、過熱度の変化に基づいて第1、第2流量調整装置6a,6bを制御する。第2流量調整装置6bは全開とされ、第1流量調整装置6aの開度が変化する。図12に示すように、空調負荷が大きくなって、循環する冷媒量が多い状態になる(S10)と、第1流量調整装置6aが全開になる(S11)。制御装置20は、各流量調整装置6a,6bの開度が所定の開度以上、例えば80%以上になったことを確認して、露付き防止制御を開始し、圧縮機1の回転数を下げるように圧縮機1を制御する(S12)。そして、制御装置20は、室外熱交換器用のファン15の回転数を下げるようにファン15を制御する(S13)。   When the air conditioning operation is performed in the cooling mode, the control device 20 controls the first and second flow rate adjusting devices 6a and 6b based on the change in the degree of superheat. The second flow rate adjusting device 6b is fully opened, and the opening degree of the first flow rate adjusting device 6a changes. As shown in FIG. 12, when the air conditioning load is increased and the amount of circulating refrigerant is large (S10), the first flow rate adjusting device 6a is fully opened (S11). The control device 20 confirms that the opening degree of each of the flow rate adjusting devices 6a and 6b is not less than a predetermined opening degree, for example, 80% or more, starts dew prevention control, and sets the rotation speed of the compressor 1. The compressor 1 is controlled to be lowered (S12). And the control apparatus 20 controls the fan 15 so that the rotation speed of the fan 15 for outdoor heat exchangers may be lowered | hung (S13).

制御装置20が圧縮機1の回転数の低下に応じて第1流量調整装置6aの開度を変更すると、第1流量調整装置6aの開度は小さくなる。圧縮機1の回転数に応じて最適な冷媒量も下がる。開度を大きくできるように第1流量調整装置6aは制御可能となるので、空調負荷が大きくても第1流量調整装置6aの開度を大きくすることができる。第1流量調整装置6aの開度を大きくすることにより、循環する冷媒量が多くなり、空調負荷が大きい状況でも、冷媒量を最適に調整することができる。これによって、室内熱交換器13における冷媒不足を解消でき、室内熱交換器13に温度むらは生じず、露付きを防止することができる。   When the control device 20 changes the opening degree of the first flow rate adjusting device 6a in accordance with the decrease in the rotational speed of the compressor 1, the opening degree of the first flow rate adjusting device 6a becomes smaller. The optimum amount of refrigerant also decreases according to the rotational speed of the compressor 1. Since the first flow rate adjustment device 6a can be controlled so that the opening degree can be increased, the opening degree of the first flow rate adjustment device 6a can be increased even if the air conditioning load is large. By increasing the opening degree of the first flow rate adjusting device 6a, the amount of circulating refrigerant increases, and the amount of refrigerant can be optimally adjusted even in a situation where the air conditioning load is large. As a result, the shortage of refrigerant in the indoor heat exchanger 13 can be solved, temperature unevenness does not occur in the indoor heat exchanger 13, and dew condensation can be prevented.

圧縮機1の回転数が下がると同時に、室外熱交換器用のファン15の回転数を下げることにより、室外熱交換器14に向かう風速が弱まり、室外熱交換器14での冷媒の放熱が減る。室外熱交換器14に溜まる冷媒が減ることにより、循環する冷媒量が多くなり、冷媒不足を補うことができる。圧縮機1の回転数を下げるだけの場合に比べて、循環する冷媒量を多くすることが可能となる。すなわち、圧縮機1の回転数の下げ幅を小さくしても、冷媒不足を解消できるだけの冷媒量を確保することができる。空調能力は圧縮機1の回転数に比例するので、圧縮機1の回転数の低下が小さいほど空調能力の低下を抑えることができる。したがって、室内熱交換器13に十分な冷媒が流れ、過熱度を小さくすることができ、空調負荷が大きくても効率よく空調運転することができる。   At the same time as the rotation speed of the compressor 1 is decreased, the rotation speed of the fan 15 for the outdoor heat exchanger is decreased, so that the wind speed toward the outdoor heat exchanger 14 is weakened, and the heat radiation of the refrigerant in the outdoor heat exchanger 14 is decreased. By reducing the amount of refrigerant that accumulates in the outdoor heat exchanger 14, the amount of refrigerant that circulates increases, and the shortage of refrigerant can be compensated. Compared with the case where only the rotational speed of the compressor 1 is reduced, the amount of circulating refrigerant can be increased. That is, even if the amount of decrease in the rotational speed of the compressor 1 is reduced, it is possible to secure an amount of refrigerant that can solve the shortage of refrigerant. Since the air conditioning capacity is proportional to the rotational speed of the compressor 1, the smaller the decrease in the rotational speed of the compressor 1, the lower the decrease in the air conditioning capacity. Therefore, sufficient refrigerant flows through the indoor heat exchanger 13, the degree of superheat can be reduced, and the air conditioning operation can be performed efficiently even when the air conditioning load is large.

なお、上記では、各流量調整装置6の開度が全開あるいは全開近くになったとき、制御装置20は循環する冷媒量が多い状態であると判断して、露付き防止制御を開始する。この代わりに、制御装置20は、空調負荷が大きいとき、循環する冷媒量が多い状態になったことを検知して、露付き防止制御を行ってもよい。すなわち、冷房モード時に、制御装置20は、外気温と室内熱交換器13の温度を検出し、これらの情報に基づいて循環する冷媒量が多い状態であるかを判断する。外気温が所定温度以上で蒸発器4(室内熱交換器13)の温度あるいは圧縮機1の吐出温度あるいはサクション温度が所定温度以上になったとき、制御装置20は、循環する冷媒量が多い状態であると判断する。この状態になったとき、各流量調整装置6の開度は所定の開度以上になっている。   In the above description, when the opening degree of each flow rate adjustment device 6 becomes fully open or close to full open, the control device 20 determines that the amount of circulating refrigerant is large and starts dew prevention control. Instead, when the air conditioning load is large, the control device 20 may detect that the amount of circulating refrigerant is large and perform dew prevention control. That is, in the cooling mode, the control device 20 detects the outside air temperature and the temperature of the indoor heat exchanger 13, and determines whether the amount of the circulating refrigerant is large based on these information. When the outside air temperature is equal to or higher than the predetermined temperature and the temperature of the evaporator 4 (indoor heat exchanger 13) or the discharge temperature or the suction temperature of the compressor 1 is equal to or higher than the predetermined temperature, the control device 20 has a large amount of refrigerant to circulate. It is judged that. When this state is reached, the opening degree of each flow rate adjusting device 6 is greater than or equal to a predetermined opening degree.

また、過熱度が大きくなり、流量調整装置6の開度が全開あるいは全開近くになったときに、凝縮器2用のファンの回転数だけを下げるようにしてもよい。凝縮器2の熱交換能力が低下するので、凝縮器2に溜まる冷媒が減り、循環する冷媒量を多くすることができる。したがって、冷房モード時だけでなく暖房モード時においても、流量調整装置6を全開近くまで開かなくても、循環する冷媒量を調整することができる。なお、圧縮機1の回転数が下がると同時に、凝縮器2用のファンの回転数を下げるようにしてもよい。これにより、冷房モード時だけでなく暖房モード時においても、流量調整装置6を全開近くまで開けなくても、循環する冷媒量を調整することができる。   Further, when the degree of superheat increases and the opening degree of the flow rate adjusting device 6 becomes fully open or close to full open, only the rotational speed of the fan for the condenser 2 may be lowered. Since the heat exchange capability of the condenser 2 is reduced, the amount of refrigerant accumulated in the condenser 2 is reduced, and the amount of circulating refrigerant can be increased. Therefore, not only in the cooling mode but also in the heating mode, the circulating refrigerant amount can be adjusted without opening the flow rate adjusting device 6 to near full open. In addition, you may make it reduce the rotation speed of the fan for the condenser 2 simultaneously with the rotation speed of the compressor 1 falling. Thereby, not only in the cooling mode but also in the heating mode, the amount of circulating refrigerant can be adjusted without opening the flow rate adjusting device 6 to near full open.

(第8の実施形態)
冷媒回路を循環する冷媒は、冷媒回路の接続配管7に接続された連結管8を通じてレシーバ5に出入りする。接続配管7内の冷媒の圧力とレシーバ5内の圧力との圧力差に応じて、冷媒が連結管8からレシーバ5に入って溜まったり、溜まっている冷媒がレシーバ5から排出される。この圧力差だけでは、スムーズに冷媒がレシーバ5から出入りできない。レシーバ5の温度が冷媒の温度より高いとき、レシーバ5内の圧力が高まり、冷媒はレシーバ5に流れ込みにくくなり、冷媒が溜まらない。レシーバ5の温度が冷媒の温度より低いとき、レシーバ5内の圧力が低下し、冷媒はレシーバ5から出にくくなり、レシーバ5の冷媒が減らない。
(Eighth embodiment)
The refrigerant circulating in the refrigerant circuit enters and exits the receiver 5 through the connecting pipe 8 connected to the connection pipe 7 of the refrigerant circuit. Depending on the pressure difference between the pressure of the refrigerant in the connection pipe 7 and the pressure in the receiver 5, the refrigerant enters the receiver 5 from the connecting pipe 8 and accumulates, or the accumulated refrigerant is discharged from the receiver 5. The refrigerant cannot smoothly enter and exit from the receiver 5 only with this pressure difference. When the temperature of the receiver 5 is higher than the temperature of the refrigerant, the pressure in the receiver 5 increases, the refrigerant becomes difficult to flow into the receiver 5, and the refrigerant does not accumulate. When the temperature of the receiver 5 is lower than the temperature of the refrigerant, the pressure in the receiver 5 decreases, the refrigerant becomes difficult to get out of the receiver 5, and the refrigerant in the receiver 5 does not decrease.

そこで、本実施形態では、冷媒がスムーズにレシーバ5に出入りできるように、レシーバ5を暖めたり、冷やしたりする。図13,図14に示すように、冷媒回路から低温の冷媒を分流させてレシーバ5を冷却する冷却管30と、冷媒回路から高温の冷媒を分流させてレシーバ5を温める加熱管31とが設けられる。加熱管31は、圧縮機1の吐出側の配管に接続され、冷却管30は、圧縮機1の吸入側の配管に接続される。冷却管30および加熱管31は、互いに接触しないようにレシーバ5に巻き付けられる。なお、その他の構成および動作は上記の各実施形態と同じである。   Therefore, in the present embodiment, the receiver 5 is warmed or cooled so that the refrigerant can smoothly enter and exit the receiver 5. As shown in FIGS. 13 and 14, a cooling pipe 30 that cools the receiver 5 by diverting a low-temperature refrigerant from the refrigerant circuit, and a heating pipe 31 that warms the receiver 5 by diverting a high-temperature refrigerant from the refrigerant circuit are provided. It is done. The heating pipe 31 is connected to a discharge side pipe of the compressor 1, and the cooling pipe 30 is connected to a suction side pipe of the compressor 1. The cooling pipe 30 and the heating pipe 31 are wound around the receiver 5 so as not to contact each other. Other configurations and operations are the same as those in the above embodiments.

冷却管30および加熱管31は、それぞれ1本のキャピラリチューブから形成され、冷媒回路の配管よりも小径とされる。冷却管30の一端および他端が冷媒回路の配管にそれぞれ連通し、一端側および他端側に、冷却管30を開閉する冷却弁32がそれぞれ設けられる。同様に加熱管31の一端および他端が冷媒回路の配管にそれぞれ連通し、一端側および他端側に、加熱管31を開閉する加熱弁33がそれぞれ設けられる。   The cooling pipe 30 and the heating pipe 31 are each formed from a single capillary tube and have a smaller diameter than the piping of the refrigerant circuit. One end and the other end of the cooling pipe 30 communicate with the piping of the refrigerant circuit, respectively, and cooling valves 32 for opening and closing the cooling pipe 30 are provided on one end side and the other end side, respectively. Similarly, one end and the other end of the heating pipe 31 communicate with the piping of the refrigerant circuit, respectively, and heating valves 33 for opening and closing the heating pipe 31 are provided on one end side and the other end side, respectively.

冷却弁32および加熱弁33は、運転状況に応じて制御装置20によって制御される。2つの冷却弁32が同時に開くと、冷却管30に低温の冷媒が流れる。2つの冷却弁32が閉じているとき、冷却管30には冷媒は流れない。また、2つの加熱弁33が同時に開くと、加熱管31に高温の冷媒が流れる。2つの加熱弁33が閉じているとき、加熱管31には冷媒は流れない。   The cooling valve 32 and the heating valve 33 are controlled by the control device 20 according to the operating situation. When the two cooling valves 32 are simultaneously opened, a low-temperature refrigerant flows through the cooling pipe 30. When the two cooling valves 32 are closed, no refrigerant flows through the cooling pipe 30. Further, when the two heating valves 33 are opened simultaneously, a high-temperature refrigerant flows through the heating pipe 31. When the two heating valves 33 are closed, no refrigerant flows through the heating pipe 31.

レシーバ5に冷媒を溜めるとき、制御装置20は、冷却弁32を開き、加熱弁33を閉じる。圧縮機1に吸い込まれる低温の冷媒が冷却管30に流れ込み、レシーバ5は冷やされる。レシーバ5内のガス冷媒が液化して、レシーバ5内の圧力が下がり、冷媒回路の配管側の圧力とレシーバ5内の圧力との差が大きくなる。圧力差が大きくなった分、冷媒がスムーズにレシーバ5に流れ込み、冷媒が早く溜まる。したがって、循環する冷媒量をすばやく少なくすることができる。   When storing the refrigerant in the receiver 5, the control device 20 opens the cooling valve 32 and closes the heating valve 33. The low-temperature refrigerant sucked into the compressor 1 flows into the cooling pipe 30 and the receiver 5 is cooled. The gas refrigerant in the receiver 5 is liquefied, the pressure in the receiver 5 is lowered, and the difference between the pressure on the piping side of the refrigerant circuit and the pressure in the receiver 5 is increased. As the pressure difference increases, the refrigerant smoothly flows into the receiver 5 and accumulates quickly. Therefore, the amount of circulating refrigerant can be quickly reduced.

レシーバ5から冷媒を排出するとき、制御装置20は、冷却弁32を閉じ、加熱弁33を開く。圧縮機1から吐出された高温の冷媒が加熱管31に流れ込み、レシーバ5は暖められる。レシーバ5内の液冷媒が蒸発して、レシーバ5内の圧力が高まり、レシーバ5内の圧力と冷媒回路の配管側との差が大きくなる。圧力差が大きくなった分、冷媒がスムーズにレシーバ5から流れ出し、冷媒が早く排出される。したがって、循環する冷媒量をすばやく増やすことができる。   When discharging the refrigerant from the receiver 5, the control device 20 closes the cooling valve 32 and opens the heating valve 33. The high-temperature refrigerant discharged from the compressor 1 flows into the heating pipe 31, and the receiver 5 is warmed. The liquid refrigerant in the receiver 5 evaporates, the pressure in the receiver 5 increases, and the difference between the pressure in the receiver 5 and the piping side of the refrigerant circuit increases. As the pressure difference increases, the refrigerant flows out of the receiver 5 smoothly and is discharged quickly. Therefore, the amount of circulating refrigerant can be increased quickly.

冷却管30および加熱管31は極細管とされる。冷媒回路の配管から冷媒がそれぞれの管30,31に流れても、循環する冷媒量の減少は少しだけである。したがって、空調能力に影響を及ぼすことなく、レシーバ5の温度調節が可能となる。そして、流量調整装置6の制御に連動して、レシーバ5の温度調節を行うことにより、レシーバ5への冷媒の出入りがスムーズになり、循環する冷媒量をすばやく最適に調整することができる。   The cooling pipe 30 and the heating pipe 31 are very thin tubes. Even if the refrigerant flows from the piping of the refrigerant circuit to the respective pipes 30 and 31, the amount of the circulating refrigerant is reduced only slightly. Therefore, the temperature of the receiver 5 can be adjusted without affecting the air conditioning capability. Then, by adjusting the temperature of the receiver 5 in conjunction with the control of the flow rate adjusting device 6, the refrigerant flows into and out of the receiver 5 smoothly, and the amount of circulating refrigerant can be adjusted quickly and optimally.

なお、冷媒回路が複数のレシーバ5を有している場合でも、各レシーバ5に冷却管30および加熱管31を巻き付ければよい。また、複数のレシーバ5のうち、冷媒が出入りしないレシーバ5に対しては、冷却弁32および加熱弁33は閉じたままにしておく。これにより、冷媒回路を循環する冷媒をむやみに減らさずにすむ。   Even when the refrigerant circuit has a plurality of receivers 5, the cooling pipe 30 and the heating pipe 31 may be wound around each receiver 5. Moreover, the cooling valve 32 and the heating valve 33 are kept closed with respect to the receiver 5 in which a refrigerant | coolant does not enter / exit among several receivers 5. FIG. Thereby, it is not necessary to reduce the refrigerant circulating through the refrigerant circuit.

ところで、実開昭59−118984号公報に記載のように、レシーバ5に冷媒回路の配管を直接巻き付けることが考えられる。しかし、運転モードに応じた温度の冷媒しか流れず、運転状況に応じて高温の冷媒と低温の冷媒とを切り替えることができず、冷媒量の調整には適さない。   By the way, as described in Japanese Utility Model Publication No. 59-118984, it is conceivable to directly wrap the pipe of the refrigerant circuit around the receiver 5. However, only the refrigerant having a temperature corresponding to the operation mode flows, and the high-temperature refrigerant and the low-temperature refrigerant cannot be switched according to the operation state, which is not suitable for adjusting the refrigerant amount.

(第9の実施形態)
レシーバ5は、室外機11内の隙間に配置されている。レシーバ5の配置を決めるとき、レシーバ5および連結管8が室外機11内の配管や部品に干渉しないように考慮しなければならない。一方、レシーバ5は所定の容積を確保するため、レシーバ5の大きさや形状が決められる。しかし、室外機11内には、構造上、限られた隙間しかなく、干渉しないようにレシーバ5を配置するには、配管や部品のレイアウトを変更したり、さらには室外機11を大きくしたりして、レシーバ5を配置できる隙間を確保する必要がある。
(Ninth embodiment)
The receiver 5 is disposed in a gap in the outdoor unit 11. When deciding the arrangement of the receiver 5, consideration must be given so that the receiver 5 and the connecting pipe 8 do not interfere with the piping and components in the outdoor unit 11. On the other hand, the size and shape of the receiver 5 are determined in order to ensure a predetermined volume of the receiver 5. However, in the outdoor unit 11, there is only a limited gap due to the structure, and in order to arrange the receiver 5 so as not to interfere, the layout of piping and parts is changed, or the outdoor unit 11 is enlarged. Thus, it is necessary to secure a gap in which the receiver 5 can be disposed.

そこで、本実施形態では、図15〜17に示すように、レシーバ5が複数のタンク40から構成される。ここでは、1つのレシーバ5は3つのタンク40から構成される。なお、その他の構成および動作は上記の各実施形態と同じである。   Therefore, in the present embodiment, the receiver 5 includes a plurality of tanks 40 as shown in FIGS. Here, one receiver 5 is composed of three tanks 40. Other configurations and operations are the same as those in the above embodiments.

タンク40は、円筒状の容器であり、底面に出入口が形成され、各タンク40は同じ形状とされる。3つのタンク40の容積の合計は、1つのレシーバ5の容積と同じである。各タンク40は、室外機11内の隙間に位置し、互いに接触することなく、ずらされて配置される。図17に示すように、3つのタンク40は、1本の連結管8に枝管41を介してそれぞれ連通される。タンク40の下面に枝管41が接続され、枝管41は連結管8に接続される。タンク40は枝管41よりも高い位置にあり、各枝管41の上下方向の位置はそれぞれ異なる。   The tank 40 is a cylindrical container, and an entrance is formed on the bottom surface. The tanks 40 have the same shape. The total volume of the three tanks 40 is the same as the volume of one receiver 5. Each tank 40 is located in a gap in the outdoor unit 11 and is shifted and arranged without contacting each other. As shown in FIG. 17, the three tanks 40 are respectively connected to one connecting pipe 8 through branch pipes 41. A branch pipe 41 is connected to the lower surface of the tank 40, and the branch pipe 41 is connected to the connecting pipe 8. The tank 40 is located higher than the branch pipe 41, and the vertical positions of the branch pipes 41 are different.

レシーバ5に冷媒を溜めるとき、冷媒は、冷媒回路の配管から連結管8に流れ込み、最も低い位置に接続された枝管41を通じてタンク40に入る。続いて、冷媒は、この枝管41よりも高い位置に接続された枝管41から他のタンク40に入る。冷媒は、低い位置の枝管41に接続されたタンク40からに順に溜まっていく。   When the refrigerant is stored in the receiver 5, the refrigerant flows from the pipe of the refrigerant circuit into the connecting pipe 8 and enters the tank 40 through the branch pipe 41 connected to the lowest position. Subsequently, the refrigerant enters the other tank 40 from the branch pipe 41 connected to a position higher than the branch pipe 41. The refrigerant accumulates in order from the tank 40 connected to the branch pipe 41 at the lower position.

レシーバ5から冷媒が排出されるとき、冷媒は高い位置にあるほど位置エネルギが大きいので、最も高い位置にあるタンク40に溜まっている冷媒がまず排出される。冷媒は、高い位置にあるタンク40から順に排出される。   When the refrigerant is discharged from the receiver 5, the higher the position of the refrigerant is, the higher the potential energy is. Therefore, the refrigerant stored in the tank 40 at the highest position is discharged first. The refrigerant is sequentially discharged from the tank 40 at a high position.

このように、タンク40はレシーバ5に比べて小さくなるので、タンク40を収容できる隙間は小さくてよい。そのため、タンク40を配置できる位置の選択肢が増える。したがって、室外機11内の配管や部品の配置を変更することなく、隙間に応じてレシーバ5を配置することができる。しかも、レシーバ5用の大きな隙間を形成する必要がないので、室外機11の小型化も図れる。   Thus, since the tank 40 is smaller than the receiver 5, the gap that can accommodate the tank 40 may be small. Therefore, the choice of the position where the tank 40 can be arranged increases. Therefore, the receiver 5 can be arranged according to the gap without changing the arrangement of the pipes and components in the outdoor unit 11. Moreover, since it is not necessary to form a large gap for the receiver 5, the outdoor unit 11 can be downsized.

また、配管や部品のレイアウトにより、必然的に隙間が形成されるが、隙間の形状は多様なものとなる。そこで、隙間の形状に応じてタンク40の形状を変えてもよい。例えば、図18に示すように、タンク40がL形に形成される。これにより、タンク40の設置可能なスペースが増え、室外機11内のスペースを有効に活用でき、室外機11をより一層小型化できる。   In addition, gaps are inevitably formed depending on the layout of piping and parts, but the shapes of the gaps are various. Therefore, the shape of the tank 40 may be changed according to the shape of the gap. For example, as shown in FIG. 18, the tank 40 is formed in an L shape. Thereby, the space which can install the tank 40 increases, the space in the outdoor unit 11 can be utilized effectively, and the outdoor unit 11 can be further reduced in size.

レシーバ5が複数ある場合でも、同様に各レシーバ5を複数のタンク40で構成してもよい。なお、全てのレシーバ5を複数のタンク40から構成する必要はなく、レシーバ5を設置できる隙間がある場合は、そのままレシーバ5を用いてもよい。   Even when there are a plurality of receivers 5, each receiver 5 may be configured with a plurality of tanks 40. Note that it is not necessary to configure all the receivers 5 from a plurality of tanks 40. If there is a gap in which the receivers 5 can be installed, the receivers 5 may be used as they are.

(第10の実施形態)
図9に示すような、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6a,6bとを有する空気調和機において、流量調整装置6a,6bを制御する制御装置20は、冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置6a,6bの開度を制御する。
(Tenth embodiment)
In an air conditioner having a receiver 5 for storing refrigerant and a plurality of flow rate adjusting devices 6a and 6b for adjusting the amount of refrigerant stored in the receiver 5 in order to adjust the amount of refrigerant circulating in the refrigerant circuit, as shown in FIG. The control device 20 that controls the flow rate adjusting devices 6a and 6b controls the opening degree of the flow rate adjusting devices 6a and 6b so that the refrigerant amount circulating in the refrigerant circuit becomes the optimum refrigerant amount according to the air conditioning operation.

ここで、空調運転が開始されたとき、圧縮機1が駆動され、冷媒が冷媒回路を循環することにより冷凍サイクルが形成される。設定温度と室温に基づいて圧縮機1の目標回転数が設定され、目標回転数に応じて各流量調整装置6a,6bの初期開度が決められる。   Here, when the air conditioning operation is started, the compressor 1 is driven, and the refrigerant circulates through the refrigerant circuit to form a refrigeration cycle. The target rotational speed of the compressor 1 is set based on the set temperature and the room temperature, and the initial opening degree of each flow rate adjusting device 6a, 6b is determined according to the target rotational speed.

空調運転が開始されると、各流量調整装置6a,6bは初期開度まで開かれ、圧縮機1が目標回転数で駆動される。圧縮機1から吐出された冷媒が冷媒回路を循環して、しばらくすると冷凍サイクルが安定する。この後、室温や外気温に応じて圧縮機1の回転数が変更され、圧縮機1の回転数に応じて各流量調整装置6a,6bの開度が変更され、循環する冷媒量が最適になるように調整される。   When the air conditioning operation is started, the flow rate adjusting devices 6a and 6b are opened to the initial opening degree, and the compressor 1 is driven at the target rotational speed. The refrigerant discharged from the compressor 1 circulates through the refrigerant circuit, and after a while, the refrigeration cycle is stabilized. Thereafter, the rotation speed of the compressor 1 is changed according to the room temperature or the outside air temperature, the opening degree of each flow rate adjusting device 6a, 6b is changed according to the rotation speed of the compressor 1, and the amount of circulating refrigerant is optimized. It is adjusted to become.

制御装置20は、冷凍サイクルが安定したことを確認してから、冷媒量調整制御を行う。従来では、特許第3334507号公報に記載のように、圧縮機1からの冷媒の吐出温度が所定温度以上になったか否かにより、冷凍サイクルの安定性が判断されていた。しかし、外気温の変化や圧縮機1の回転数の変化により、吐出温度も変化する。そのため、冷凍サイクルがまだ安定していないにもかかわらず、吐出温度が所定温度に達することがあり、誤った判断がされる。その結果、最適な冷媒量になるまでの時間が余計にかかってしまう。   The controller 20 performs refrigerant amount adjustment control after confirming that the refrigeration cycle is stable. Conventionally, as described in Japanese Patent No. 3334507, the stability of the refrigeration cycle is determined based on whether or not the discharge temperature of the refrigerant from the compressor 1 is equal to or higher than a predetermined temperature. However, the discharge temperature also changes due to a change in the outside air temperature or a change in the rotation speed of the compressor 1. Therefore, even though the refrigeration cycle is not yet stable, the discharge temperature may reach a predetermined temperature, and an erroneous determination is made. As a result, it takes extra time to reach the optimum refrigerant amount.

そこで、本実施形態では、冷凍サイクルが安定したことを厳密に判断できるように、制御装置20は、圧縮機1の吐出温度の変化を表す数式を用いて冷凍サイクルが安定したか否かを判断し、冷凍サイクルが安定してから流量調整装置6の開度の制御を行う。このとき、圧縮機1の回転数をパラメータとした複数の数式が用意され、制御装置20は、圧縮機1の回転数に応じて、判断のために用いる数式を選択する。   Therefore, in the present embodiment, the control device 20 determines whether or not the refrigeration cycle is stable using a mathematical expression that represents a change in the discharge temperature of the compressor 1 so that it can be strictly determined that the refrigeration cycle is stable. Then, the opening degree of the flow rate adjusting device 6 is controlled after the refrigeration cycle is stabilized. At this time, a plurality of mathematical expressions are prepared using the rotation speed of the compressor 1 as a parameter, and the control device 20 selects a mathematical expression to be used for determination according to the rotation speed of the compressor 1.

冷凍サイクルの安定性の判断は、圧縮機1からの吐出温度の時間変化に基づいて行われる。この判断に用いられる数式は、吐出温度の時間変化を測定した結果から得られる近似式とされ、数式には、圧縮機1の回転数、吐出温度、外気温がパラメータとして加味されている。なお、吐出温度は、圧縮機1の出口側に接続された吐出管の表面温度とされる。   The determination of the stability of the refrigeration cycle is made based on the change over time in the discharge temperature from the compressor 1. The mathematical formula used for this determination is an approximate formula obtained from the result of measuring the change in discharge temperature over time, and the rotational speed of the compressor 1, the discharge temperature, and the outside air temperature are taken into account in the mathematical formula. The discharge temperature is the surface temperature of the discharge pipe connected to the outlet side of the compressor 1.

安定性の判断処理のフローを図19に示す。まず、圧縮機1の吐出温度の時間変化が実測され、予め設定された数式Aと実測値とから近似式A1が作成される(S20)。この近似式A1が制御装置20のメモリに記憶される。そして、空調運転が開始されると、制御装置20は、検出された外気温および圧縮機1の回転数を近似式A1に入力する(S21)。制御装置20は、圧縮機1の吐出温度と外気温との温度差ΔTの時間変化の度合いが所定値δの範囲内か否かを判断する(S22)。この処理が繰り返され、温度差ΔTの時間変化の度合いが所定値δの範囲内になったとき、制御装置20は、冷凍サイクルが安定したと判断して(S23)、安定性の判断処理を終了する。   FIG. 19 shows a flow of stability determination processing. First, the time change of the discharge temperature of the compressor 1 is actually measured, and the approximate expression A1 is created from the preset numerical expression A and the actual measurement value (S20). This approximate expression A1 is stored in the memory of the control device 20. When the air conditioning operation is started, the control device 20 inputs the detected outside air temperature and the rotation speed of the compressor 1 to the approximate expression A1 (S21). The control device 20 determines whether or not the degree of time change of the temperature difference ΔT between the discharge temperature of the compressor 1 and the outside air temperature is within a predetermined value δ (S22). When this process is repeated and the degree of time change of the temperature difference ΔT is within the range of the predetermined value δ, the control device 20 determines that the refrigeration cycle is stable (S23), and performs the stability determination process. finish.

次に、近似式の具体的な作成手順を示す。本実施形態では、異なる回転数に対して、それぞれ近似式が作成される。   Next, a specific procedure for creating an approximate expression is shown. In the present embodiment, approximate expressions are created for different rotational speeds.

(ステップ1)
外気温Tout1のときに、回転数f1、f2で圧縮機1を回転させたときの安定時吐出温度および回転数f1、f2で圧縮機1を回転させたときの吐出温度が測定される。図20(a)は、回転数f1、f2における吐出温度の時間変化を示す。縦軸は、吐出温度と外気温との温度差ΔT、横軸は、時間tを表わす。図中、ΔT1は回転数f1のときの安定時吐出温度Td11−Tout、ΔT2は回転数f2のときの安定時吐出温度Td12−Toutである。Toutは任意の外気温である。このプロットした実測値から明らかなように、温度差関数ΔT(t)は、時間の経過と共にそれぞれΔT1およびΔT2に収束する形になる。また、圧縮機1の回転数が高いほど吐出温度が高くなるので、回転数が高いときの温度差は、回転数が低いときの温度差よりも大きくなる。
(Step 1)
At the outside air temperature Tout1, the stable discharge temperature when the compressor 1 is rotated at the rotation speeds f1 and f2 and the discharge temperature when the compressor 1 is rotated at the rotation speeds f1 and f2 are measured. FIG. 20A shows the change over time in the discharge temperature at the rotation speeds f1 and f2. The vertical axis represents the temperature difference ΔT between the discharge temperature and the outside air temperature, and the horizontal axis represents time t. In the figure, ΔT1 is the stable discharge temperature Td11-Tout at the rotation speed f1, and ΔT2 is the stable discharge temperature Td12-Tout at the rotation speed f2. Tout is an arbitrary outside temperature. As is apparent from the plotted actual measurement values, the temperature difference function ΔT (t) converges to ΔT1 and ΔT2 with time. Moreover, since discharge temperature becomes high, so that the rotation speed of the compressor 1 is high, the temperature difference when the rotation speed is high becomes larger than the temperature difference when the rotation speed is low.

(ステップ2)
吐出温度の時間変化に関する数式が予め設定され、制御装置20のメモリに記憶される。数式は、回転数毎に式Aおよび式aが作成される。
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ1)} ・・・(式A)
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ2)} ・・・(式a)
f:任意の回転数
τ1、τ2:パラメータ
式Aにおいて、f=f1とすると、
ΔT(t)=ΔT1×{1−e(−t/τ1)} ・・・(式A´)
式aにおいて、f=f2とすると、
ΔT(t)=ΔT2×{1−e(−t/τ2)} ・・・(式a´)
(Step 2)
Formulas relating to changes in the discharge temperature over time are set in advance and stored in the memory of the control device 20. Formulas A and a are created for each rotation speed.
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ1) } (Formula A)
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ2) } (Formula a)
f: Arbitrary rotational speed τ1, τ2: parameter In Formula A, if f = f1,
ΔT (t) = ΔT1 × {1-e (−t / τ1) } (Expression A ′)
In formula a, if f = f2,
ΔT (t) = ΔT2 × {1-e (−t / τ2) } (Expression a ′)

(ステップ3)
ステップ1での測定結果と最小二乗法により、パラメータτ1、τ2が決められる。図20(b)に示すように、パラメータτの値により、ΔT(t)の飽和曲線の傾きが大きく異なる。この図より、プロットした測定値に最も近似する曲線として、τ=3.5の曲線が挙げられる。また、圧縮機1の回転数が異なると、パラメータτの値は異なる。
(Step 3)
Parameters τ1 and τ2 are determined by the measurement result in step 1 and the least square method. As shown in FIG. 20B, the slope of the saturation curve of ΔT (t) varies greatly depending on the value of the parameter τ. From this figure, a curve of τ = 3.5 is given as a curve that most closely approximates the plotted measurement values. Further, when the rotation speed of the compressor 1 is different, the value of the parameter τ is different.

ここまでの手順により決まった値が式A、式aに代入され、以下の式A、式aのアンダーライン部分が決まる。
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ1)} ・・・(式A)
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ2)} ・・・(式a)
図20(c)に式Aの飽和曲線を示す。圧縮機1の回転数によって飽和曲線が変化することがわかる。
The values determined by the procedure so far are substituted into Formula A and Formula a, and the underlined portion of Formula A and Formula a below is determined.
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ1) } (Formula A)
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ2) } (Formula a)
FIG. 20C shows a saturation curve of the formula A. It can be seen that the saturation curve changes depending on the rotational speed of the compressor 1.

(ステップ4)
外気温がTout2のときに回転数f1、f2で圧縮機1を回転させたときの安定時吐出温度および回転数f1、f2で圧縮機1を回転させたときの安定時吐出温度Td21、Td22が測定される。外気温は吐出温度に影響を及ぼす。そこで、外気温による吐出温度の変化度合に基づいて式A、式aにおけるΔT1、ΔT2を補正することにより、外気温の影響をなくすことができ、吐出温度の時間変化に対する正確な近似式が得られる。
(Step 4)
When the outside air temperature is Tout2, the stable discharge temperature when the compressor 1 is rotated at the rotation speeds f1 and f2, and the stable discharge temperature Td21 and Td22 when the compressor 1 is rotated at the rotation speeds f1 and f2 are Measured. The outside air temperature affects the discharge temperature. Therefore, by correcting ΔT1 and ΔT2 in the expressions A and a based on the change degree of the discharge temperature due to the outside air temperature, the influence of the outside air temperature can be eliminated, and an accurate approximate expression for the time change of the discharge temperature can be obtained. It is done.

(ステップ5)
ステップ4での回転数f1のときの測定結果が式Bに代入される。また、回転数f2のときの測定結果が式Cに代入される。
ΔT1=Td11+(Td21−Td11)
×(Tout−Tout1)/(Tout2−Tout1)
−Tout1 ・・・式B
ΔT2=Td12+(Td22−Td12)
×(Tout−Tout1)/(Tout2−Tout1)
−Tout1 ・・・式C
式B、式Cが式A、式aにそれぞれ代入され、近似式A1、a1が得られる。
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ1)} ・・・(式A1)
ΔT(t)={ΔT2+(ΔT1−ΔT2)×(f−f2)/(f1−f2)}
×{1−e(−t/τ2)} ・・・(式a1)
上式のΔT1、ΔT2には、式B、式Cが使用される。図21(a)に、外気温によって吐出温度の飽和曲線が変化することを示す。
(Step 5)
The measurement result at the rotation speed f1 in step 4 is substituted into equation B. Further, the measurement result at the rotation speed f2 is substituted into the expression C.
ΔT1 = Td11 + (Td21−Td11)
× (Tout-Tout1) / (Tout2-Tout1)
−Tout1 Formula B
ΔT2 = Td12 + (Td22−Td12)
× (Tout-Tout1) / (Tout2-Tout1)
−Tout1 Formula C
Expressions B and C are substituted into Expression A and Expression a, respectively, and approximate expressions A1 and a1 are obtained.
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ1) } (Formula A1)
ΔT (t) = {ΔT2 + (ΔT1−ΔT2) × (f−f2) / (f1−f2)}
X {1-e (-t / τ2) } (Formula a1)
Expressions B and C are used for ΔT1 and ΔT2 in the above expressions. FIG. 21A shows that the discharge temperature saturation curve changes depending on the outside air temperature.

上記のようにして得られた2つの近似式は、圧縮機1の回転数に対応したものである。すなわち、近似式a1が、圧縮機1の回転数が所定回転数より高い高回転域に対応し、近似式A1が、所定回転数より低い低回転域に対応する。   The two approximate expressions obtained as described above correspond to the rotational speed of the compressor 1. That is, the approximate expression a1 corresponds to a high rotation range where the rotation speed of the compressor 1 is higher than the predetermined rotation speed, and the approximate expression A1 corresponds to a low rotation speed range lower than the predetermined rotation speed.

これらの近似式は制御装置20のメモリに記憶され、冷凍サイクルの安定性の判断に用いられる。すなわち、制御装置20は、空調運転を開始すると、2つの近似式から選択された一方の近似式に圧縮機1の回転数と検出された外気温を代入して、運転開始からの時間毎の温度差を算出する。なお、圧縮機1の回転数は、圧縮機1のモータの回転数を検出することによって取得される、あるいは圧縮機1を駆動するときに出力される運転周波数に基づいて取得される。   These approximate expressions are stored in the memory of the control device 20 and are used to determine the stability of the refrigeration cycle. That is, when starting the air conditioning operation, the control device 20 substitutes the rotation speed of the compressor 1 and the detected outside air temperature into one of the approximate equations selected from the two approximate equations, and each time since the start of the operation. Calculate the temperature difference. The rotational speed of the compressor 1 is acquired by detecting the rotational speed of the motor of the compressor 1 or is acquired based on the operating frequency output when the compressor 1 is driven.

そして、制御装置20は、算出した温度差の変化が小さくなるタイミングを演算する。温度差の変化が小さくなったタイミングが、冷凍サイクルが安定したときと判断される。制御装置20は、このタイミングになるときの時間を近似式から導き出す。この時間が、運転開始から安定するまでに要する安定時間とされる。制御装置20は、運転を開始してから安定時間に達すると、冷凍サイクルが安定したと判断して、冷媒量調整制御を行う。   And the control apparatus 20 calculates the timing when the change of the calculated temperature difference becomes small. It is determined that the timing at which the change in the temperature difference becomes small is when the refrigeration cycle is stabilized. The control device 20 derives the time when this timing is reached from the approximate expression. This time is defined as a stabilization time required from the start of operation to stabilization. The control device 20 determines that the refrigeration cycle is stable when the stable time is reached after starting the operation, and performs refrigerant amount adjustment control.

安定時間に達するまでに、外気温が変化したとき、制御装置20は、再度演算を行って、安定時間を修正する。圧縮機1の回転数が変更されたときも、同様に安定時間が修正される。   When the outside air temperature changes before reaching the stable time, the control device 20 performs the calculation again to correct the stable time. When the rotational speed of the compressor 1 is changed, the stabilization time is similarly corrected.

具体的には、任意の回転数fと外気温Toutをそれぞれ代入した式A1あるいは式a1において、ΔT(t)の時間変化率が閾値δよりも小さくなったとき、冷凍サイクルが安定したと判断される(図21(b)参照)。閾値δは、例えば、±0.1℃/minとされる。なお、この閾値はあくまでも例示であって、これに限定されるものではない。   Specifically, in Formula A1 or Formula a1 into which an arbitrary rotation speed f and outside air temperature Tout are respectively substituted, it is determined that the refrigeration cycle is stable when the time change rate of ΔT (t) becomes smaller than the threshold δ. (See FIG. 21B). The threshold δ is, for example, ± 0.1 ° C./min. This threshold value is merely an example, and is not limited to this.

ここで、2つの近似式のうち一方の近似式が圧縮機1の回転数に応じて選択される。一方の近似式a1が高回転域に対応し、他方の近似式A1が低回転域に対応する。制御装置20は、運転時の回転数が高回転域にあるか低回転域にあるかを判別し、回転域に対応する近似式を選択する。このように、安定性の判断に用いる近似式を圧縮機1の回転数に応じて使い分けることにより、より厳密な判断を行うことができる。しかも、安定性の判断は、運転中に検出された圧縮機1の吐出温度に基づいて行うものではない。そのため、実際の吐出温度の変動に左右されることなく、安定性の判断を行うことができ、判断の信頼性が高まる。   Here, one of the two approximate expressions is selected according to the rotational speed of the compressor 1. One approximate expression a1 corresponds to the high rotation range, and the other approximate expression A1 corresponds to the low rotation range. The control device 20 determines whether the rotation speed during operation is in a high rotation range or a low rotation range, and selects an approximate expression corresponding to the rotation range. In this way, a more rigorous determination can be made by properly using the approximate expression used for the determination of stability according to the rotational speed of the compressor 1. In addition, the determination of stability is not performed based on the discharge temperature of the compressor 1 detected during operation. Therefore, the stability can be determined without being influenced by the actual change in the discharge temperature, and the reliability of the determination is increased.

なお、判断に用いる近似式は、2つ以上であってもよい。圧縮機1の回転数に対して、複数の回転域が設定され、複数の近似式が各回転域に対応する。運転時の回転数が属する回転域に応じた近似式が選択される。また、レシーバ5は1つに限らず、複数のレシーバ5であってもよい。   Note that the number of approximate equations used for the determination may be two or more. A plurality of rotation ranges are set with respect to the rotation speed of the compressor 1, and a plurality of approximate expressions correspond to the respective rotation ranges. An approximate expression is selected according to the rotation range to which the rotation speed during operation belongs. Further, the number of receivers 5 is not limited to one, and a plurality of receivers 5 may be used.

以上の通り、本発明の空気調和機は、圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備えたものである。絞り部3は、冷媒を溜める複数のレシーバ5と、冷媒回路を循環する冷媒量を調整するために各レシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成される。   As described above, the air conditioner of the present invention includes a refrigerant circuit in which the compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are connected by piping. The throttling unit 3 includes a plurality of receivers 5 that store refrigerant and a plurality of flow rate adjusting devices 6 that adjust the amount of refrigerant stored in each receiver 5 in order to adjust the amount of refrigerant circulating in the refrigerant circuit.

各レシーバ5に溜まる冷媒量によって、冷媒回路を循環する冷媒量が変わる。そこで、運転状況に応じて流量調整装置6が動作することにより、各レシーバ5に溜まる冷媒量が調整され、運転状況に応じた最適な冷媒量にすることができる。   The amount of refrigerant circulating in the refrigerant circuit varies depending on the amount of refrigerant accumulated in each receiver 5. Therefore, by operating the flow rate adjusting device 6 according to the operating state, the refrigerant amount accumulated in each receiver 5 is adjusted, and the optimum refrigerant amount according to the operating state can be obtained.

冷媒回路に複数の流量調整装置6が直列に配され、隣り合う流量調整装置6の間にレシーバ5が接続され、レシーバ5よりも冷媒の流れ方向の下流側に位置する流量調整装置6が動作することにより、レシーバ5に溜まる冷媒量が変化する。   A plurality of flow rate adjusting devices 6 are arranged in series in the refrigerant circuit, a receiver 5 is connected between the adjacent flow rate adjusting devices 6, and the flow rate adjusting device 6 located downstream of the receiver 5 in the refrigerant flow direction operates. As a result, the amount of refrigerant accumulated in the receiver 5 changes.

流量調整装置6の動作により、下流側に位置するレシーバ5に溜まる冷媒量を調整でき、上流側に位置するレシーバ6では、冷媒は溜まらない。このように、複数の流量調整装置6を動作させることにより、レシーバ5毎に溜まる冷媒量を調整することが可能となり、循環する冷媒量を運転状況に応じた最適な量にすることができる。   The operation of the flow rate adjusting device 6 can adjust the amount of refrigerant accumulated in the receiver 5 located on the downstream side, and no refrigerant accumulates in the receiver 6 located on the upstream side. As described above, by operating the plurality of flow rate adjusting devices 6, it is possible to adjust the amount of refrigerant accumulated for each receiver 5, and the amount of circulating refrigerant can be set to an optimum amount according to the operation state.

流量調整装置6の開度を制御する制御装置20が設けられ、制御装置20は、少なくとも1つの流量調整装置6の開度を制御し、他の流量調整装置6を全開にする。   A control device 20 for controlling the opening degree of the flow rate adjusting device 6 is provided, and the control device 20 controls the opening degree of at least one flow rate adjusting device 6 to fully open the other flow rate adjusting device 6.

制御対象の流量調整装置6よりも下流側に位置するレシーバ5では、溜まる冷媒量が調整可能とされ、上流側に位置するレシーバ5には、冷媒は溜まらない。したがって、制御対象の流量調整装置6に応じて、冷媒が溜まるレシーバ5が決まり、運転状況に応じて制御対象の流量調整装置6を制御することにより、全レシーバ5に溜まる冷媒量が変わり、循環する冷媒量を最適な冷媒量にすることができる。   In the receiver 5 located on the downstream side of the flow rate adjusting device 6 to be controlled, the amount of refrigerant accumulated can be adjusted, and no refrigerant accumulates in the receiver 5 located on the upstream side. Therefore, the receiver 5 in which the refrigerant accumulates is determined according to the flow rate adjustment device 6 to be controlled, and the amount of refrigerant accumulated in all the receivers 5 is changed by controlling the flow rate adjustment device 6 as the control object according to the operation status, and is circulated. The amount of refrigerant to be made can be made the optimum amount of refrigerant.

このとき、制御装置20は、制御対象以外の他の流量調整装置6を全開にした後、制御対象の流量調整装置6を制御する。このような流量調整装置6の動作順にすることにより、レシーバ5に冷媒が溜まっているとき、レシーバ5から冷媒が急に排出されるようなことが起こっても、冷媒は他の流量調整装置6をスムーズに通過する。   At this time, the control device 20 controls the flow control device 6 to be controlled after fully opening the flow control device 6 other than the control target. By arranging the operation order of the flow rate adjusting device 6 as described above, even if the refrigerant is suddenly discharged from the receiver 5 when the refrigerant is accumulated in the receiver 5, the refrigerant is not in the other flow rate adjusting device 6. Pass through smoothly.

各レシーバ5の容積が異なるものとされる。複数のレシーバ5のうち、少なくとも1つのレシーバ5の容積が異なっていればよい。運転状況に応じて冷媒を溜めるレシーバ5を選ぶことにより、全レシーバ5に溜める冷媒量を運転状況に応じて最適にすることができる。   The volume of each receiver 5 is different. The volume of at least one receiver 5 among the plurality of receivers 5 may be different. By selecting the receiver 5 that stores the refrigerant in accordance with the operating conditions, the amount of refrigerant stored in all the receivers 5 can be optimized in accordance with the operating conditions.

室内熱交換器13を備えた室内機10と室外熱交換器14を備えた室外機11とから構成された空気調和機において、室内熱交換器13の容積が室外熱交換器14の容積よりも小さいとき、室外熱交換器14に近いレシーバ5の容積が室内熱交換器13に近いレシーバ5の容積より小さくされ、室外熱交換器14の容積が室内熱交換器13の容積よりも小さいとき、室外熱交換器14に近いレシーバ5の容積が室内熱交換器13に近いレシーバ5の容積より大きくされる。これにより、冷媒過多の状態での運転を避けることができ、最適な冷媒量での運転がしやすくなる。   In the air conditioner configured by the indoor unit 10 including the indoor heat exchanger 13 and the outdoor unit 11 including the outdoor heat exchanger 14, the volume of the indoor heat exchanger 13 is larger than the volume of the outdoor heat exchanger 14. When the volume is small, the volume of the receiver 5 near the outdoor heat exchanger 14 is smaller than the volume of the receiver 5 near the indoor heat exchanger 13, and when the volume of the outdoor heat exchanger 14 is smaller than the volume of the indoor heat exchanger 13, The volume of the receiver 5 close to the outdoor heat exchanger 14 is made larger than the volume of the receiver 5 close to the indoor heat exchanger 13. As a result, operation in an excessive refrigerant state can be avoided, and operation with an optimal amount of refrigerant is facilitated.

凝縮器2に近い位置に設けられたレシーバ5の容積が他のレシーバ5の容積よりも小とされる。容積の小さいレシーバ5に冷媒を溜めたとき、循環する冷媒量を多くすることができる。特に、循環する冷媒量を多くする運転モードでは、凝縮器2に近い位置にあるレシーバ5の上流側にある流量調整装置6を制御することにより、容積の小さいレシーバ5に溜まる冷媒を早く調整でき、簡単に循環する冷媒量を多くすることができる。   The volume of the receiver 5 provided at a position close to the condenser 2 is made smaller than the volume of the other receivers 5. When the refrigerant is stored in the receiver 5 having a small volume, the amount of the circulating refrigerant can be increased. In particular, in the operation mode in which the amount of refrigerant circulating is increased, the refrigerant accumulated in the receiver 5 having a small volume can be quickly adjusted by controlling the flow rate adjusting device 6 on the upstream side of the receiver 5 located near the condenser 2. Therefore, it is possible to easily increase the amount of refrigerant circulating.

冷媒の流れ方向の上流側に位置するレシーバ5の容積は、下流側に位置するレシーバ5の容積よりも小とされる。すなわち、上流側から下流側に向かって容積の小さい順にレシーバ5が配置される。これにより、循環する冷媒量を最適にするための各流量調整装置6の制御を容易に行える。   The volume of the receiver 5 located on the upstream side in the refrigerant flow direction is smaller than the volume of the receiver 5 located on the downstream side. That is, the receivers 5 are arranged in ascending order of volume from the upstream side toward the downstream side. Thereby, control of each flow control device 6 for optimizing the amount of circulating refrigerant can be easily performed.

レシーバ5は1つの出入口を備え、冷媒回路から分岐した連結管8がレシーバ5の出入口に接続され、隣り合う流量調整装置6の間に連結管8が配される。レシーバ5の入口と出口を別々にする場合に比べて、連結管8が1本ですむ。そのため、レシーバ5が複数であっても、配管が増えすぎることがなく、レシーバ5の設置スペースを容易に確保できる。   The receiver 5 includes one inlet / outlet, a connecting pipe 8 branched from the refrigerant circuit is connected to the inlet / outlet of the receiver 5, and the connecting pipe 8 is arranged between the adjacent flow rate adjusting devices 6. Compared to the case where the inlet and outlet of the receiver 5 are separated, only one connecting pipe 8 is required. For this reason, even if there are a plurality of receivers 5, the number of pipes does not increase and the installation space for the receiver 5 can be easily secured.

圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備え、絞り部3は、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成され、冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置6の開度を制御する制御装置20が設けられ、複数の流量調整装置6の開度が所定の開度以上になったとき、制御装置20は、圧縮機1の回転数を下げる。このとき、制御装置20は、制御対象以外の流量調整装置6を所定の開度以上にしてから、制御対象の流量調整装置6を制御して所定の開度以上にする。   The compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are provided with a refrigerant circuit that is connected by piping, and the throttle unit 3 adjusts the amount of refrigerant that circulates in the refrigerant circuit and the receiver 5 that stores the refrigerant. The flow rate adjusting device 6 is configured so that the amount of refrigerant circulating in the refrigerant circuit becomes the optimum amount of refrigerant according to the air conditioning operation. When the control device 20 to be controlled is provided and the opening amounts of the plurality of flow rate adjusting devices 6 are equal to or greater than a predetermined opening amount, the control device 20 decreases the rotational speed of the compressor 1. At this time, the control device 20 sets the flow rate adjustment device 6 other than the control target to a predetermined opening degree or more, and then controls the control target flow rate adjustment device 6 to the predetermined opening degree or more.

循環する冷媒量が不足するとき、流量調整装置6が全開近くまで開いていると、これ以上対処できないが、圧縮機1の回転数を下げることにより、流量調整装置6の開度が小さくなるように変更される。これにより、流量調整装置6の開度を制御することが可能となり、冷媒不足を解消できる。   When the amount of refrigerant circulating is insufficient, if the flow rate adjusting device 6 is open to the fully open position, it cannot be dealt with any more. However, by reducing the rotation speed of the compressor 1, the opening degree of the flow rate adjusting device 6 is reduced. Changed to Thereby, it becomes possible to control the opening degree of the flow control device 6, and it is possible to eliminate the shortage of refrigerant.

圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備え、絞り部3は、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成され、冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置6の開度を制御する制御装置20が設けられ、制御装置20は、複数の流量調整装置6の開度を所定の開度以上にして圧縮機1の回転数を下げたとき、凝縮器2に向かって送風するファン15の回転数を下げる。   The compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are provided with a refrigerant circuit that is connected by piping, and the throttle unit 3 adjusts the amount of refrigerant that circulates in the refrigerant circuit and the receiver 5 that stores the refrigerant. The flow rate adjusting device 6 is configured so that the amount of refrigerant circulating in the refrigerant circuit becomes the optimum amount of refrigerant according to the air conditioning operation. A control device 20 for controlling is provided, and the control device 20 blows air toward the condenser 2 when the opening degree of the plurality of flow rate adjustment devices 6 is set to a predetermined opening degree or more and the rotational speed of the compressor 1 is reduced. The rotational speed of the fan 15 is lowered.

複数の流量調整装置6の開度が所定の開度以上であるとき、冷媒不足による露付きを防止するために、圧縮機1の回転数が下げられ、さらに凝縮器用のファン15の回転数が下げられる。圧縮機1の回転数だけを下げた場合に比べて、循環する冷媒量をより多くすることができる。すばやく冷媒不足が解消され、露付きを防止できる。   When the opening degree of the plurality of flow rate adjusting devices 6 is equal to or greater than a predetermined opening degree, the rotation speed of the compressor 1 is reduced and the rotation speed of the condenser fan 15 is further reduced in order to prevent dew condensation due to insufficient refrigerant. Be lowered. Compared with the case where only the rotation speed of the compressor 1 is lowered, the amount of circulating refrigerant can be increased. The shortage of refrigerant can be quickly resolved and dew can be prevented.

圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備え、絞り部3は、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成され、冷媒回路から低温の冷媒を分流させてレシーバ5を冷却する冷却管30と、冷媒回路から高温の冷媒を分流させてレシーバ5を温める加熱管31とが設けられる。   The compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are provided with a refrigerant circuit that is connected by piping, and the throttle unit 3 adjusts the amount of refrigerant that circulates in the refrigerant circuit and the receiver 5 that stores the refrigerant. And a plurality of flow rate adjusting devices 6 for adjusting the amount of refrigerant stored in the receiver 5, and a cooling pipe 30 that cools the receiver 5 by diverting a low-temperature refrigerant from the refrigerant circuit, and a high-temperature refrigerant from the refrigerant circuit. And a heating tube 31 that warms the receiver 5.

低温の冷媒によりレシーバ5が冷却されると、レシーバ5に冷媒が流入しやすくなる。高温の冷媒によりレシーバ5を温めると、冷媒がレシーバ5から排出されやすくなる。これにより、冷媒がレシーバ5に対してスムーズに出入りする。   When the receiver 5 is cooled by the low-temperature refrigerant, the refrigerant easily flows into the receiver 5. When the receiver 5 is warmed by the high-temperature refrigerant, the refrigerant is easily discharged from the receiver 5. As a result, the refrigerant smoothly enters and exits the receiver 5.

冷却管30を開閉する冷却弁32と加熱管31を開閉する加熱弁33とが設けられ、レシーバ5に冷媒を溜めるとき、冷却弁32が開かれて加熱弁33が閉じられ、レシーバ5から冷媒を排出するとき、冷却弁32が閉じられて加熱弁33が開かれる。   A cooling valve 32 that opens and closes the cooling pipe 30 and a heating valve 33 that opens and closes the heating pipe 31 are provided. When the refrigerant is accumulated in the receiver 5, the cooling valve 32 is opened and the heating valve 33 is closed. Is discharged, the cooling valve 32 is closed and the heating valve 33 is opened.

制御装置20は、運転状況に応じて冷却弁32および加熱弁33を制御する。冷却弁32および加熱弁33が流量調整装置6に連動して制御されることにより、レシーバ5に対する冷媒の出入りがスムーズに行われ、循環する冷媒量をすばやく調整することができる。   The control device 20 controls the cooling valve 32 and the heating valve 33 according to the operation status. By controlling the cooling valve 32 and the heating valve 33 in conjunction with the flow rate adjusting device 6, the refrigerant flows in and out of the receiver 5 smoothly, and the amount of circulating refrigerant can be quickly adjusted.

加熱管31は、圧縮機1の吐出側の配管に接続され、冷却管30は、圧縮機1の吸入側の配管に接続される。加熱管31を流れる冷媒の温度はレシーバ5内の冷媒の温度よりも高温であるので、レシーバ5内の液体冷媒を蒸発させて、内圧を上げることができ、冷媒が排出されやすくなる。冷却管30を流れる冷媒の温度はレシーバ5内の冷媒の温度よりも低温であるので、レシーバ5内のガス冷媒を液化させて、内圧を下げることができ、冷媒がレシーバ5内に流入しやすくなる。   The heating pipe 31 is connected to a discharge side pipe of the compressor 1, and the cooling pipe 30 is connected to a suction side pipe of the compressor 1. Since the temperature of the refrigerant flowing through the heating pipe 31 is higher than the temperature of the refrigerant in the receiver 5, the liquid refrigerant in the receiver 5 can be evaporated to increase the internal pressure, and the refrigerant is easily discharged. Since the temperature of the refrigerant flowing through the cooling pipe 30 is lower than the temperature of the refrigerant in the receiver 5, the gas refrigerant in the receiver 5 can be liquefied to lower the internal pressure, and the refrigerant easily flows into the receiver 5. Become.

冷却管30および加熱管31が冷媒回路の配管よりも小径の細管とされ、冷却管30および加熱管31がレシーバ5に巻き付けられる。冷媒回路から冷媒が冷却管30あるいは加熱管31に流れるが、循環する冷媒量の減少を少しだけにすることができる。   The cooling pipe 30 and the heating pipe 31 are narrow pipes smaller in diameter than the piping of the refrigerant circuit, and the cooling pipe 30 and the heating pipe 31 are wound around the receiver 5. Although the refrigerant flows from the refrigerant circuit to the cooling pipe 30 or the heating pipe 31, the amount of circulating refrigerant can be reduced only slightly.

圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備え、絞り部3は、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成され、レシーバ5が複数のタンク40から構成される。   The compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are provided with a refrigerant circuit that is connected by piping, and the throttle unit 3 adjusts the amount of refrigerant that circulates in the refrigerant circuit and the receiver 5 that stores the refrigerant. And a plurality of flow rate adjusting devices 6 that adjust the amount of refrigerant stored in the receiver 5, and the receiver 5 includes a plurality of tanks 40.

小型のタンク40を用いることができるので、小さな隙間にタンク40を配置することが可能となり、レシーバ5の配置の自由度が増す。すなわち、室外機11内の隙間に複数のタンク40が配置される。室外機11内にできる隙間を有効に活用でき、レシーバ5を設置するためにスペースを取らずにすみ、室外機11の小型化を図れる。   Since the small tank 40 can be used, the tank 40 can be arranged in a small gap, and the degree of freedom of arrangement of the receiver 5 is increased. That is, the plurality of tanks 40 are arranged in the gaps in the outdoor unit 11. The gap created in the outdoor unit 11 can be used effectively, and it is possible to reduce the size of the outdoor unit 11 without installing a space for installing the receiver 5.

冷媒配管に接続された1本の連結管8に、複数のタンク40が接続され、各タンク40は、ずらされて配置される。これにより、各タンク40に対して、順に冷媒を出し入れすることができる。   A plurality of tanks 40 are connected to one connecting pipe 8 connected to the refrigerant pipe, and the respective tanks 40 are shifted and arranged. Thereby, the refrigerant can be taken in and out in order with respect to each tank 40.

圧縮機1、凝縮器2、絞り部3、蒸発器4が配管により接続されてなる冷媒回路を備え、絞り部3は、冷媒を溜めるレシーバ5と、冷媒回路を循環する冷媒量を調整するためにレシーバ5に溜める冷媒量を調整する複数の流量調整装置6とから構成され、冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置6の開度を制御する制御装置20が設けられ、制御装置20は、圧縮機1の吐出温度の変化を表す数式を用いて冷凍サイクルが安定したか否かを判断し、冷凍サイクルが安定してから流量調整装置6の開度の制御を行う。   The compressor 1, the condenser 2, the throttle unit 3, and the evaporator 4 are provided with a refrigerant circuit that is connected by piping, and the throttle unit 3 adjusts the amount of refrigerant that circulates in the refrigerant circuit and the receiver 5 that stores the refrigerant. The flow rate adjusting device 6 is configured so that the amount of refrigerant circulating in the refrigerant circuit becomes the optimum amount of refrigerant according to the air conditioning operation. A control device 20 for controlling is provided, and the control device 20 determines whether or not the refrigeration cycle is stabilized by using a mathematical expression representing a change in the discharge temperature of the compressor 1, and the flow rate adjusting device after the refrigeration cycle is stabilized. The opening degree of 6 is controlled.

上記の数式を用いることにより、冷凍サイクルが安定するタイミングを精度よく判断することができる。そして、確実に冷凍サイクルが安定してから流量調整装置6の開度を制御できるので、循環する冷媒量を効率よく調整することができる。   By using the above formula, it is possible to accurately determine the timing at which the refrigeration cycle is stabilized. And since the opening degree of the flow regulating device 6 can be controlled after the refrigeration cycle is reliably stabilized, the amount of circulating refrigerant can be adjusted efficiently.

圧縮機1の回転数をパラメータとした複数の数式が用意され、制御装置20は、運転時の圧縮機1の回転数に応じて、判断のために用いる数式を選択する。圧縮機1の回転数に応じて冷凍サイクルが安定するタイミングが異なる。そこで、回転数に対応した数式を選択することにより、冷凍サイクルが安定したことを正確に判断することができる。   A plurality of mathematical formulas using the rotational speed of the compressor 1 as a parameter is prepared, and the control device 20 selects a mathematical formula to be used for determination according to the rotational speed of the compressor 1 during operation. The timing at which the refrigeration cycle is stabilized differs depending on the rotation speed of the compressor 1. Therefore, it is possible to accurately determine that the refrigeration cycle is stable by selecting a mathematical formula corresponding to the rotational speed.

なお、本発明は、上記実施形態に限定されるものではなく、本発明の範囲内で上記実施形態に多くの修正および変更を加え得ることは勿論である。流量調整装置6として、複数のキャピラリチューブを並べて、流路を切り替えるものであってもよい。また、流量調整装置6として、弁の開口面積が異なる膨張弁を用いてもよい。   In addition, this invention is not limited to the said embodiment, Of course, many corrections and changes can be added to the said embodiment within the scope of the present invention. As the flow rate adjusting device 6, a plurality of capillary tubes may be arranged to switch the flow path. Moreover, you may use the expansion valve from which the opening area of a valve differs as the flow volume adjustment apparatus 6. FIG.

複数のレシーバ5に接続される連結管8の径および長さを変えてもよい。各連結管8にも冷媒が溜まるが、溜まる冷媒量が異なる。このように、連結管8もレシーバ5の一部であるので、各レシーバ5の容積を同じにしていても、各レシーバ5の容積を異ならせることができる。レシーバ5が設置される隙間が冷媒回路の配管から離れている場合、連結管8が長くなり、その分容積が増える。レシーバ5自体の容積を変えなくても、遠い位置にあるレシーバ5の容積は、近い位置にある他のレシーバ5の容積と異なる。   The diameter and length of the connecting pipe 8 connected to the plurality of receivers 5 may be changed. Refrigerant accumulates in each connecting pipe 8, but the amount of accumulated refrigerant is different. Thus, since the connection pipe 8 is also a part of the receiver 5, even if the volume of each receiver 5 is made the same, the volume of each receiver 5 can be varied. When the gap in which the receiver 5 is installed is away from the piping of the refrigerant circuit, the connecting pipe 8 becomes longer and the volume increases accordingly. Even if the volume of the receiver 5 itself is not changed, the volume of the receiver 5 at a far position is different from the volume of other receivers 5 at a near position.

1 圧縮機
2 凝縮器
3 絞り部
4 蒸発器
5 レシーバ
6 流量調整装置
7 接続配管
8 連結管
10 室内機
11 室外機
12 四方弁
13 室内熱交換器
14 室外熱交換器
15 室外熱交換器用のファン
16 室内熱交換器用のファン
20 制御装置
21 凝縮器温度センサ
22 蒸発器温度センサ
23 吐出温度センサ
24 サクション温度センサ
25 室温センサ
26 外気温センサ
30 冷却管
31 加熱管
32 冷却弁
33 加熱弁
40 タンク
41 枝管
DESCRIPTION OF SYMBOLS 1 Compressor 2 Condenser 3 Restriction part 4 Evaporator 5 Receiver 6 Flow control device 7 Connection pipe 8 Connection pipe 10 Indoor unit 11 Outdoor unit 12 Four-way valve 13 Indoor heat exchanger 14 Outdoor heat exchanger 15 Fan for outdoor heat exchanger DESCRIPTION OF SYMBOLS 16 Fan for indoor heat exchangers 20 Controller 21 Condenser temperature sensor 22 Evaporator temperature sensor 23 Discharge temperature sensor 24 Suction temperature sensor 25 Room temperature sensor 26 Outside temperature sensor 30 Cooling pipe 31 Heating pipe 32 Cooling valve 33 Heating valve 40 Tank 41 Branch pipe

Claims (10)

圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成され、凝縮器と蒸発器とをつなぐ配管に、各レシーバと各流量調整装置とが冷媒の流れ方向に沿って交互に配されたことを特徴とする空気調和機。 A compressor, a condenser, a throttle unit, and an evaporator are provided with a refrigerant circuit that is connected by piping. The throttle unit is provided with a plurality of receivers that store the refrigerant and each receiver for adjusting the amount of refrigerant circulating in the refrigerant circuit. It is composed of a plurality of flow rate adjusting devices that adjust the amount of refrigerant to be stored , and each receiver and each flow rate adjusting device are arranged alternately along the flow direction of the refrigerant in the piping connecting the condenser and the evaporator. A featured air conditioner. 空気調和機が停止しているとき、各流量調整装置は全開され、空調運転が開始されると、レシーバよりも冷媒の流れ方向の下流側に位置する流量調整装置が動作することにより、レシーバに溜まる冷媒量が変化することを特徴とする請求項1記載の空気調和機。 When the air conditioner is stopped, each flow rate adjusting device is fully opened, and when the air conditioning operation is started , the flow rate adjusting device located downstream of the receiver in the flow direction of the refrigerant operates to The air conditioner according to claim 1, wherein the amount of refrigerant accumulated changes. 流量調整装置の開度を制御する制御装置が設けられ、制御装置は、少なくとも1つの流量調整装置の開度を制御し、他の流量調整装置を全開にすることを特徴とする請求項1または2記載の空気調和機。 The control apparatus which controls the opening degree of a flow regulating device is provided, and a control apparatus controls the opening degree of at least 1 flow regulating device, and opens the other flow regulating device fully. 2. The air conditioner according to 2. 各レシーバの容積が異なることを特徴とする請求項1〜3のいずれかに記載の空気調和機。 The volume of each receiver differs, The air conditioner in any one of Claims 1-3 characterized by the above-mentioned. 室内熱交換器を備えた室内機と室外熱交換器を備えた室外機とから構成された空気調和機において、圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成され、各レシーバの容積が異なり、室内熱交換器の容積が室外熱交換器の容積よりも小さいとき、室外熱交換器に近いレシーバの容積が室内熱交換器に近いレシーバの容積より小さくされ、室外熱交換器の容積が室内熱交換器の容積よりも小さいとき、室外熱交換器に近いレシーバの容積が室内熱交換器に近いレシーバの容積より大きくされたことを特徴とする空気調和機。 In an air conditioner composed of an indoor unit having an indoor heat exchanger and an outdoor unit having an outdoor heat exchanger, a refrigerant circuit in which a compressor, a condenser, a throttle unit, and an evaporator are connected by piping is provided. The throttle unit includes a plurality of receivers that store refrigerant, and a plurality of flow rate adjustment devices that adjust the amount of refrigerant stored in each receiver in order to adjust the amount of refrigerant circulating in the refrigerant circuit. In contrast, when the volume of the indoor heat exchanger is smaller than the volume of the outdoor heat exchanger, the volume of the receiver near the outdoor heat exchanger is made smaller than the volume of the receiver near the indoor heat exchanger, and the volume of the outdoor heat exchanger is is smaller than the volume of the indoor heat exchanger, air conditioner characterized in that the volume of the receiver near the outdoor heat exchanger is larger than the volume of the receiver near the indoor heat exchanger. 圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成され、流量調整装置の開度を制御する制御装置が設けられ、複数の流量調整装置の開度が所定の開度以上になったとき、制御装置は、圧縮機の回転数を下げることを特徴とする空気調和機。 A compressor, a condenser, a throttle unit, and an evaporator are provided with a refrigerant circuit that is connected by piping. The throttle unit is provided with a plurality of receivers that store the refrigerant and each receiver for adjusting the amount of refrigerant circulating in the refrigerant circuit. It is composed of a plurality of flow rate adjustment devices that adjust the amount of refrigerant to be stored, a control device that controls the opening degree of the flow rate adjustment device is provided, and when the opening degree of the plurality of flow rate adjustment devices is equal to or greater than a predetermined opening degree, controller, air conditioner you characterized by lowering the rotational speed of the compressor. 圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成され、流量調整装置の開度を制御する制御装置が設けられ、制御装置は、複数の流量調整装置の開度を所定の開度以上にして圧縮機の回転数を下げたとき、凝縮器に向かって送風するファンの回転数を下げることを特徴とする空気調和機。 A compressor, a condenser, a throttle unit, and an evaporator are provided with a refrigerant circuit that is connected by piping. The throttle unit is provided with a plurality of receivers that store the refrigerant and each receiver for adjusting the amount of refrigerant circulating in the refrigerant circuit. And a control device for controlling the opening degree of the flow rate adjusting device. The control device sets the opening amounts of the plurality of flow rate adjusting devices to a predetermined opening degree or more. when lowering the rotational speed of the compressor Te, air conditioner you characterized by lowering the rotational speed of the fan for blowing air toward the condenser. 圧縮機、凝縮器、絞り部、蒸発器が配管により接続されてなる冷媒回路を備え、絞り部は、冷媒を溜める複数のレシーバと、冷媒回路を循環する冷媒量を調整するために各レシーバに溜める冷媒量を調整する複数の流量調整装置とから構成され、レシーバのそれぞれが複数のタンクから構成されたことを特徴とする空気調和機。 A compressor, a condenser, a throttle unit, and an evaporator are provided with a refrigerant circuit that is connected by piping. The throttle unit is provided with a plurality of receivers that store the refrigerant and each receiver for adjusting the amount of refrigerant circulating in the refrigerant circuit. multiple is composed of a flow control device, air conditioner characterized in that each receiver is constituted of a plurality of tanks for adjusting the amount of refrigerant accumulated. 冷媒回路から低温の冷媒を分流させてレシーバを冷却する冷却管と、冷媒回路から高温の冷媒を分流させてレシーバを温める加熱管とが設けられたことを特徴とする請求項1〜のいずれかに記載の空気調和機。 A cooling pipe from the refrigerant circuit by shunting the low-temperature refrigerant for cooling the receiver, one of the claims 1-8, characterized in that the heating pipe is provided to warm the receiver by shunting the high-temperature refrigerant from the refrigerant circuit The air conditioner described in Crab. 冷媒回路を循環する冷媒量が空調運転に応じた最適冷媒量になるように、流量調整装置の開度を制御する制御装置が設けられ、制御装置は、圧縮機の吐出温度の変化を表す数式を用いて冷凍サイクルが安定したか否かを判断し、冷凍サイクルが安定してから流量調整装置の開度の制御を行うことを特徴とする請求項1〜9のいずれかに記載の空気調和機。 A control device for controlling the opening degree of the flow rate adjusting device is provided so that the refrigerant amount circulating in the refrigerant circuit becomes an optimum refrigerant amount according to the air conditioning operation, and the control device is a mathematical expression representing a change in the discharge temperature of the compressor. The air conditioning according to any one of claims 1 to 9, wherein it is determined whether or not the refrigeration cycle is stabilized by using and the opening degree of the flow rate adjusting device is controlled after the refrigeration cycle is stabilized. Machine.
JP2013226643A 2013-10-31 2013-10-31 Air conditioner Active JP6309739B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2013226643A JP6309739B2 (en) 2013-10-31 2013-10-31 Air conditioner
PCT/JP2014/071045 WO2015064172A1 (en) 2013-10-31 2014-08-08 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2013226643A JP6309739B2 (en) 2013-10-31 2013-10-31 Air conditioner

Publications (2)

Publication Number Publication Date
JP2015087065A JP2015087065A (en) 2015-05-07
JP6309739B2 true JP6309739B2 (en) 2018-04-11

Family

ID=53003788

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2013226643A Active JP6309739B2 (en) 2013-10-31 2013-10-31 Air conditioner

Country Status (2)

Country Link
JP (1) JP6309739B2 (en)
WO (1) WO2015064172A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6320639B2 (en) * 2015-07-27 2018-05-09 三菱電機株式会社 Air conditioner
US10724777B2 (en) * 2015-10-08 2020-07-28 Mitsubishi Electric Corporation Refrigeration cycle apparatus capable of performing refrigerant recovery operation and controlling blower
WO2018078729A1 (en) * 2016-10-25 2018-05-03 三菱電機株式会社 Refrigeration cycle device
CN207556037U (en) * 2017-09-08 2018-06-29 开利公司 Liquid storage device and with its heat pump system
CN111164355B (en) * 2017-10-10 2024-01-05 三菱电机株式会社 Air conditioner
CN112313458A (en) * 2018-09-12 2021-02-02 开利公司 Liquid receiver for heating, air conditioning and refrigeration systems
JP7105903B2 (en) * 2018-09-28 2022-07-25 三菱電機株式会社 refrigeration cycle equipment
JP7257151B2 (en) * 2019-01-24 2023-04-13 サンデン・リテールシステム株式会社 Cooling system
ES2961815T3 (en) 2019-03-06 2024-03-14 Mitsubishi Electric Corp Refrigeration cycle device
JP7481619B2 (en) * 2020-04-27 2024-05-13 ダイキン工業株式会社 Refrigerant recovery control device and refrigerant recovery control system
CN113587336B (en) * 2021-06-25 2022-11-04 宁波奥克斯电气股份有限公司 Air conditioner low-temperature refrigeration continuous operation control method and device and air conditioner
EP4375590A1 (en) * 2022-11-22 2024-05-29 Carrier Corporation Charge compensator for heat pump

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0756420B2 (en) * 1989-03-31 1995-06-14 新明和工業株式会社 Ultra low temperature refrigerator
JP3140908B2 (en) * 1994-05-30 2001-03-05 三菱電機株式会社 Refrigerant circulation system
JP3334507B2 (en) * 1996-09-13 2002-10-15 三菱電機株式会社 Refrigeration system device and control method for refrigeration system device
JP4465860B2 (en) * 2000-11-20 2010-05-26 株式会社富士通ゼネラル Air conditioner refrigeration equipment

Also Published As

Publication number Publication date
JP2015087065A (en) 2015-05-07
WO2015064172A1 (en) 2015-05-07

Similar Documents

Publication Publication Date Title
JP6309739B2 (en) Air conditioner
US7954333B2 (en) Air conditioner
JP4497234B2 (en) Air conditioner
KR101237216B1 (en) An air condtioner and a control method the same
EP3059515B1 (en) Air conditioner
JP4968373B2 (en) Air conditioner
US9513041B2 (en) Air conditioner
WO2009157191A1 (en) Air conditioner and method for determining the amount of refrigerant therein
US10281184B2 (en) Air conditioner
KR20130018917A (en) Control device for an air-conditioning device and air-conditioning device provided therewith
JP6148001B2 (en) Air conditioner
WO2006095571A1 (en) Refrigerator
JP5110192B1 (en) Refrigeration equipment
JP6355325B2 (en) Refrigerator and control method of refrigerator
JP5505477B2 (en) AIR CONDITIONER AND REFRIGERANT AMOUNT JUDGING METHOD FOR AIR CONDITIONER
JP5593905B2 (en) Refrigeration equipment
JP2010096396A (en) Refrigerant amount determining method of air conditioning device, and air conditioning device
JP7138801B2 (en) refrigeration cycle equipment
JP2017009269A (en) Air conditioning system
JP2013104619A (en) Air conditioning indoor unit
JP2010007996A (en) Trial operation method of air conditioner and air conditioner
US9546806B2 (en) Air conditioner
JP5245575B2 (en) Refrigerant amount determination method for air conditioner and air conditioner
JP6092606B2 (en) Air conditioner
JP2016161235A (en) Refrigeration cycle device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20160923

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20170822

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20171004

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20180220

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20180315

R150 Certificate of patent or registration of utility model

Ref document number: 6309739

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150