JP6704512B2 - Air conditioner, railway vehicle air conditioner, and air conditioner control method - Google Patents

Air conditioner, railway vehicle air conditioner, and air conditioner control method Download PDF

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JP6704512B2
JP6704512B2 JP2019509709A JP2019509709A JP6704512B2 JP 6704512 B2 JP6704512 B2 JP 6704512B2 JP 2019509709 A JP2019509709 A JP 2019509709A JP 2019509709 A JP2019509709 A JP 2019509709A JP 6704512 B2 JP6704512 B2 JP 6704512B2
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refrigerant
compressor
pressure
air conditioner
opening degree
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JPWO2018180985A1 (en
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和平 新宮
和平 新宮
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Mitsubishi Electric Corp
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    • 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
    • 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
    • F25B49/022Compressor control arrangements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B61RAILWAYS
    • B61DBODY DETAILS OR KINDS OF RAILWAY VEHICLES
    • B61D27/00Heating, cooling, ventilating, or air-conditioning
    • 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
    • F25B1/00Compression machines, plants or systems with non-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
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/027Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means
    • F25B2313/02741Compression machines, plants or systems with reversible cycle not otherwise provided for characterised by the reversing means using one four-way valve
    • 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
    • F25B2500/00Problems to be solved
    • F25B2500/28Means for preventing liquid refrigerant entering into the compressor
    • 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
    • F25B2600/02Compressor control
    • F25B2600/026Compressor control by controlling unloaders
    • F25B2600/0262Compressor control by controlling unloaders internal to the compressor
    • 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
    • F25B2600/2501Bypass 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
    • F25B2600/2513Expansion 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
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/19Pressures
    • F25B2700/193Pressures of the compressor
    • F25B2700/1933Suction pressures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2115Temperatures of a compressor or the drive means therefor
    • F25B2700/21151Temperatures of a compressor or the drive means therefor at the suction side of the compressor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2115Temperatures of a compressor or the drive means therefor
    • F25B2700/21152Temperatures of a compressor or the drive means therefor at the discharge side of the compressor

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

Description

本発明は、空気調和装置、鉄道車両用空気調和装置および空気調和装置の制御方法に関する。 The present invention relates to an air conditioner, an air conditioner for a railway vehicle, and a control method for the air conditioner.

空気調和装置では、室内熱交換器で効率よく熱交換できるように、冷媒圧力と冷媒温度から算出した過熱度に基づいて膨張弁の開度を調整し、冷媒流通量を適切な値に維持している。膨張弁には、冷媒流通量を精度よく制御可能な電子制御式のものが広く使用されている(例えば、特許文献1参照)。 In the air conditioner, the degree of opening of the expansion valve is adjusted based on the degree of superheat calculated from the refrigerant pressure and the refrigerant temperature so that heat can be efficiently exchanged in the indoor heat exchanger, and the refrigerant flow rate is maintained at an appropriate value. ing. As the expansion valve, an electronically controlled expansion valve that can accurately control the flow rate of the refrigerant is widely used (for example, see Patent Document 1).

特開平10− 38350号公報(段落[0023]、図2参照)JP-A-10-38350 (paragraph [0023], see FIG. 2)

ところで、空気調和装置には、冷暖房能力を調整するため、圧縮機の容量を制御する容量制御機構が広く適用されている。このような容量制御機構としては、圧縮機の容量を無段階に制御可能なインバータ式容量制御機構と、主に2段階に制御可能な機械式容量制御機構とが挙げられる。 By the way, a capacity control mechanism for controlling the capacity of the compressor is widely applied to the air conditioner in order to adjust the cooling and heating capacity. Examples of such a capacity control mechanism include an inverter type capacity control mechanism capable of controlling the capacity of the compressor steplessly and a mechanical capacity control mechanism capable of controlling mainly in two steps.

このような容量制御機構を備える空気調和装置では、圧縮機の容量を変更すると、過渡的に圧縮機の吸入圧力や冷媒圧力が変動する。例えば、圧縮機の容量を低下させると、圧縮機からの冷媒排出量が減少するため、圧縮機の吸入圧力が増加し、室内熱交換器の冷媒流通量が一時的に増加する。室内熱交換器の冷媒流通量が増加すると、室内熱交換器で蒸発できなかった冷媒が圧縮機に戻る液バックが発生するおそれがある。 In the air conditioner including such a capacity control mechanism, when the capacity of the compressor is changed, the suction pressure and the refrigerant pressure of the compressor fluctuate transiently. For example, when the capacity of the compressor is reduced, the refrigerant discharge amount from the compressor decreases, so that the suction pressure of the compressor increases and the refrigerant flow amount of the indoor heat exchanger temporarily increases. When the amount of refrigerant flowing through the indoor heat exchanger increases, there is a possibility that liquid refrigerant that could not be evaporated in the indoor heat exchanger will return to the compressor, causing liquid back.

上述したように、冷媒流通量は一般に過熱度に基づいて調整されているが、過熱度の算出に使用される各種センサには、検出精度の向上を目的として、ある程度大きい時定数が設定されているため、圧縮機の容量の変化の影響が過熱度の変動として現れるまでには、時間的なずれが発生する。このため、特許文献1に記載の方法では、圧縮機の容量を変更したことで圧縮機の吸入圧力や冷媒圧力が過渡的に変動しても、この変動が過熱度の変動として検出され膨張弁の開度が変更される前に、液バックが発生するおそれがある。
特に、このような変動は、回転数をきめ細かく制御可能なインバータ式よりも、機械式容量制御機構を備える圧縮機において顕著である。
As described above, the refrigerant flow rate is generally adjusted based on the degree of superheat, but various sensors used to calculate the degree of superheat have a somewhat large time constant set for the purpose of improving detection accuracy. Therefore, a time lag occurs until the influence of the change in the capacity of the compressor appears as a change in the degree of superheat. Therefore, in the method described in Patent Document 1, even if the suction pressure and the refrigerant pressure of the compressor fluctuate transiently by changing the capacity of the compressor, this fluctuation is detected as a fluctuation of the degree of superheat and the expansion valve There is a possibility that liquid back may occur before the opening degree of is changed.
In particular, such a variation is more remarkable in a compressor provided with a mechanical displacement control mechanism than in an inverter type in which the rotational speed can be finely controlled.

本発明は上述のような課題を解決するためになされたもので、圧縮機の容量を変更することによる液バックの発生を従来よりも抑制することができる空気調和装置および鉄道車両用空気調和装置を得ることを目的とする。 The present invention has been made to solve the above problems, and an air conditioner and a rail vehicle air conditioner capable of suppressing the occurrence of liquid back due to a change in the capacity of a compressor as compared with the conventional air conditioner. Aim to get.

本発明に係る空気調和装置は、圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、前記バイパス通路を開閉するバイパス弁と、冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、前記制御装置は、前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御にて設定される開度に対して所定開度だけ小さい値に補正する制限処理を開始し、前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果に基づき前記所定開度を設定するものである。
本発明に係る空気調和装置は、圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、前記バイパス通路を開閉するバイパス弁と、冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、前記制御装置は、前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御にて設定される値よりも小さい値に補正する制限処理を開始し、前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果が第1所定圧力以上であることを前記制限処理の開始条件とするものである。
本発明に係る空気調和装置の制御方法は、圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路と、前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、前記バイパス通路を開閉するバイパス弁と、を備えた空気調和装置の制御方法であって、冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御工程と、前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御工程にて設定される開度に対して所定開度だけ小さい値に補正する制限工程と、を備え、前記所定開度は、前記圧縮機に流入する冷媒の圧力に基づき設定されるものである。
The air conditioner according to the present invention, a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve the air conditioning apparatus having a refrigerant circuit connected with refrigerant pipes, the compressor an intermediate compression chamber refrigerant in the process of compression are present, a bypass passage connecting the low-pressure space in which the refrigerant of the refrigerant by Ri low pressure in the intermediate compression chambers is present, a bypass valve that opens and closes the bypass passage, overheating of the refrigerant And a control device that performs superheat degree control that sets the opening degree of the electronic expansion valve based on the degree, and the control device is based on the bypass valve being switched from the closed state to the open state. Te, the limit processing for correcting a small value by a predetermined degree of opening of the electronic expansion valve against opening that will be set by the superheat control begin, the control device, the compressor The predetermined opening degree is set based on the detection result of the pressure detecting means for detecting the pressure of the inflowing refrigerant .
An air conditioner according to the present invention is an air conditioner having a refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger, and an electronic expansion valve are connected by a refrigerant pipe, and the compressor is in the middle of compression. Of the intermediate compression chamber in which the refrigerant exists, a bypass passage that communicates with a low-pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber exists, a bypass valve that opens and closes the bypass passage, and based on the degree of superheat of the refrigerant. And a controller for performing superheat control for setting the opening degree of the electronic expansion valve, wherein the controller is based on the bypass valve being switched from a closed state to an open state. Pressure control means for starting a limiting process for correcting the opening degree of the expansion valve to a value smaller than the value set by the superheat control, and the control device detecting the pressure of the refrigerant flowing into the compressor. The condition for starting the limiting process is that the detection result of 1 is equal to or higher than the first predetermined pressure.
A control method for an air conditioner according to the present invention, a compressor, an outdoor heat exchanger, an indoor heat exchanger and a refrigerant circuit in which an electronic expansion valve is connected by a refrigerant pipe, and a refrigerant in the middle of compression of the compressor exists. A method of controlling an air conditioner comprising: a bypass passage that communicates the intermediate compression chamber with a low-pressure space in which a refrigerant having a pressure lower than that of the refrigerant in the intermediate compression chamber exists; and a bypass valve that opens and closes the bypass passage. A superheat control step of setting the opening degree of the electronic expansion valve based on the degree of superheat of the refrigerant, and the electronic expansion based on the bypass valve being switched from the closed state to the open state. A restriction step of correcting the opening degree of the valve to a value smaller than the opening degree set in the superheat degree control step by a predetermined opening degree, the predetermined opening degree of the refrigerant flowing into the compressor. It is set based on the pressure.

本発明に係る空気調和装置は、圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間と連通するバイパス通路と、前記バイパス通路を開閉するバイパス弁と、冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、前記制御装置は、前記バイパス弁を開弁状態から閉弁状態に切り換える切り換え要求を検出すると、前記電子膨張弁の開度を前記過熱度制御にて設定される開度に対して所定開度だけ大きい値に補正する促進処理を開始し、その後、前記バイパス弁を開弁状態から閉弁状態に切り換え、前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果に基づき前記所定開度を設定するものである。
本発明に係る空気調和装置の制御方法は、圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路と、前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間と連通するバイパス通路と、前記バイパス通路を開閉するバイパス弁と、を備えた空気調和装置の制御方法であって、冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御工程と、前記バイパス弁を開弁状態から閉弁状態に切り換える切り換え要求を検出すると、前記電子式膨張弁の開度を前記過熱度制御工程にて設定される開度に対して所定開度だけ大きい値に補正する促進工程と、を備え、前記所定開度は、前記圧縮機に流入する冷媒の圧力に基づき設定されるものである。
An air conditioner according to the present invention is an air conditioner having a refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger, and an electronic expansion valve are connected by a refrigerant line, and the compressor is in the middle of compression. The intermediate compression chamber in which the refrigerant exists, the bypass passage communicating with the low-pressure space in which the refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber, the bypass valve opening and closing the bypass passage, and the superheat of the refrigerant and a control device for implementing the superheat degree control that sets the degree of opening of the electronic expansion valve, wherein the control unit detects the change request to switch to the closed state the bypass valve from the open state, the electronic expansion start the promotion processing for correcting to a large value by a predetermined degree the opening of the valve against the opening that will be set by the superheat degree control, then conversion cut in the closed state of the bypass valve from the open state In addition, the control device sets the predetermined opening degree based on the detection result of the pressure detection means for detecting the pressure of the refrigerant flowing into the compressor .
A control method for an air conditioner according to the present invention, a compressor, an outdoor heat exchanger, an indoor heat exchanger and a refrigerant circuit in which an electronic expansion valve is connected by a refrigerant line, and a refrigerant in the middle of compression of the compressor is present. A method for controlling an air conditioner, comprising: an intermediate compression chamber, a bypass passage communicating with a low-pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber exists, and a bypass valve opening and closing the bypass passage. , A superheat control step of setting the opening degree of the electronic expansion valve based on the degree of superheat of the refrigerant, and a switching request for switching the bypass valve from the open state to the closed state is detected, And an accelerating step of correcting the opening to a value larger than the opening set in the superheat control step by a predetermined opening, wherein the predetermined opening is the pressure of the refrigerant flowing into the compressor. It is set based on.

本発明によれば、バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、電子式膨張弁の開度を過熱度制御にて設定される値よりも小さい値に補正するため、圧縮機の容量の変化が過熱度の変動に反映される前に、冷媒流通量を低下させることができる。このため、圧縮機の容量を変更することによる液バックの発生を従来よりも抑制することができる。 According to the present invention, the opening degree of the electronic expansion valve is corrected to a value smaller than the value set by the superheat control based on the switching of the bypass valve from the closed state to the open state. The amount of refrigerant flow can be reduced before the change in the capacity of the compressor is reflected in the change in the degree of superheat. Therefore, the occurrence of liquid back due to the change in the capacity of the compressor can be suppressed more than ever before.

圧縮機の容量を上昇させると、圧縮機からの冷媒排出量が増加するため、圧縮機内の冷媒量が一時的に減少する。圧縮機内の冷媒量が減少すると、圧縮機内の摺動部が直接に接触摺動し、焼き付き等の不具合が発生する可能性がある。この点、本発明によれば、バイパス弁を開弁状態から閉弁状態に切り換える前に、電子式膨張弁の開度を過熱度制御にて設定される値よりも大きい値に補正する促進処理を開始するため、圧縮機内に貯留される冷媒量を増加させることができる。このため、バイパス弁を開弁状態から閉弁状態に切り換えることに起因して圧縮機内の冷媒量が急減することを抑制することができる。従って、摺動部が直接に接触摺動し、焼き付き等の不具合が発生することを抑制することができる。 When the capacity of the compressor is increased, the amount of refrigerant discharged from the compressor increases, so the amount of refrigerant in the compressor temporarily decreases. When the amount of refrigerant in the compressor decreases, the sliding portion in the compressor may directly contact and slide, which may cause a problem such as seizure. In this respect, according to the present invention, before the bypass valve is switched from the open state to the closed state, the acceleration process for correcting the opening degree of the electronic expansion valve to a value larger than the value set by the superheat control. Therefore, the amount of refrigerant stored in the compressor can be increased. Therefore, it is possible to prevent the amount of refrigerant in the compressor from rapidly decreasing due to switching the bypass valve from the open state to the closed state. Therefore, it is possible to prevent the sliding portion from directly contacting and sliding to cause a defect such as seizure.

本発明の実施の形態1にかかる空気調和装置の模式図である。It is a schematic diagram of the air conditioning apparatus concerning Embodiment 1 of this invention. 本発明の実施の形態1にかかる圧縮機および容量制御機構の断面図である。It is a sectional view of a compressor and a capacity control mechanism concerning Embodiment 1 of the present invention. 本発明の実施の形態1にかかる空気調和装置の制御フローチャートである。It is a control flowchart of the air conditioning apparatus concerning Embodiment 1 of this invention. 本発明の実施の形態1にかかる空気調和装置の制限処理および促進処理による電子式膨張弁の開度、検出温度と設定温度、冷媒圧力および運転モードの変化を説明するタイミングチャートである。5 is a timing chart for explaining changes in the opening degree of the electronic expansion valve, the detected temperature and the set temperature, the refrigerant pressure, and the operation mode due to the limiting process and the promoting process of the air-conditioning apparatus according to Embodiment 1 of the present invention. 本発明の実施の形態2にかかる空気調和装置の制御フローチャートである。It is a control flowchart of the air conditioning apparatus concerning Embodiment 2 of this invention. 本発明の実施の形態2にかかる空気調和装置の制限処理および促進処理による電子式膨張弁の開度、検出温度と設定温度、冷媒圧力および運転モードの変化を説明するタイミングチャートである。6 is a timing chart for explaining changes in the opening degree of the electronic expansion valve, the detected temperature and the set temperature, the refrigerant pressure, and the operation mode due to the restriction process and the acceleration process of the air conditioner according to the second embodiment of the present invention. 本発明の実施の形態3にかかる空気調和装置の制御フローチャートである。It is a control flowchart of the air conditioning apparatus concerning Embodiment 3 of this invention. 本発明の実施の形態4にかかる鉄道車両の模式図である。It is a schematic diagram of the railway vehicle concerning Embodiment 4 of this invention. 本発明の実施の形態4にかかる圧縮機の側面図である。It is a side view of the compressor concerning Embodiment 4 of the present invention. 本発明の他の実施の形態にかかる空気調和装置の模式図である。It is a schematic diagram of the air conditioning apparatus concerning other embodiment of this invention.

本発明を実施するための形態について添付の図面を参照しながら説明する。なお、各図中、同一または相当する部分には同一の符号を付しており、その重複説明は適宜に簡略化ないし省略する。また説明の便宜上、各図中に示す部分のサイズ、形状の比例関係等が誇張されている場合がある。 Embodiments for carrying out the present invention will be described with reference to the accompanying drawings. In the drawings, the same or corresponding parts are designated by the same reference numerals, and the duplicate description thereof will be appropriately simplified or omitted. Further, for convenience of description, the proportional relationship between the size and shape of the parts shown in each drawing may be exaggerated.

(実施の形態1)
図1〜図4を参照しながら、本発明の実施の形態1にかかる空気調和装置10について説明する。本実施の形態にかかる空気調和装置10は、図1に示すように、冷媒を圧縮する圧縮機1と、冷媒を減圧させる電子式膨張弁2と、冷房運転時に凝縮器として機能し、室外の空気と冷媒との熱交換を行う室外熱交換器3と、冷房運転時に蒸発器として機能し、室内の空気と冷媒との熱交換を行う室内熱交換器4と、これらを制御する制御装置7とを有する。制御装置7には、空気調和装置10が設けられた室内の温度を測定する室温センサ14、およびユーザが空気調和装置10のオンオフ制御や所望の設定温度Toの入力を行うリモコン15が接続されている。
(Embodiment 1)
The air conditioning apparatus 10 according to Embodiment 1 of the present invention will be described with reference to FIGS. 1 to 4. As shown in FIG. 1, an air conditioner 10 according to the present embodiment functions as a compressor 1 that compresses a refrigerant, an electronic expansion valve 2 that depressurizes the refrigerant, and a condenser during cooling operation, and the outdoor unit. An outdoor heat exchanger 3 for exchanging heat between air and refrigerant, an indoor heat exchanger 4 for exchanging heat between indoor air and refrigerant during cooling operation, and a controller 7 for controlling these. Have and. The controller 7 is connected to a room temperature sensor 14 that measures the temperature of the room in which the air conditioner 10 is installed, and a remote controller 15 that allows the user to perform on/off control of the air conditioner 10 and input a desired set temperature To. There is.

圧縮機1は、吸入した冷媒を圧縮し、高温・高圧の状態にして吐出する。本実施の形態における圧縮機1は、機械式の容量制御機構60を備えるスクロール圧縮機から構成され、単位時間(秒)あたり、予め定められた一定の圧縮回数で運転される。容量制御機構60の詳細については後述する。 The compressor 1 compresses the sucked refrigerant, discharges it in a high temperature/high pressure state. The compressor 1 in the present embodiment is composed of a scroll compressor including a mechanical capacity control mechanism 60, and is operated at a predetermined fixed number of compressions per unit time (second). Details of the capacity control mechanism 60 will be described later.

室外熱交換器3は、室外から取り込まれた外気と冷媒との間で熱交換を行う外気用の熱交換器であり、冷房時に冷媒から外気に熱を移動する。
室内熱交換器4は、室内空気と冷媒との間で熱交換を行う室内用の熱交換器であり、冷房時に室内空気から冷媒に熱を移動する。
The outdoor heat exchanger 3 is a heat exchanger for the outside air that exchanges heat between the outside air taken from the outside and the refrigerant, and transfers heat from the refrigerant to the outside air during cooling.
The indoor heat exchanger 4 is an indoor heat exchanger that performs heat exchange between the indoor air and the refrigerant, and transfers heat from the indoor air to the refrigerant during cooling.

電子式膨張弁2は、冷媒を減圧して膨張させ、低温低圧の冷媒とするものであり、開度が可変に制御可能な膨張弁で構成されている。好ましくは、電子リニア膨張弁(Linear Expansion Valve:LEV)が用いられている。 The electronic expansion valve 2 decompresses and expands the refrigerant to obtain a low-temperature low-pressure refrigerant, and is composed of an expansion valve whose opening can be variably controlled. Preferably, an electronic linear expansion valve (LEV) is used.

圧縮機1、室外熱交換器3、電子式膨張弁2および室内熱交換器4は冷媒が流通する冷媒管路20で接続され、冷媒が循環する冷媒回路を構成する。冷房運転時、冷媒は、図1の実線矢印に示す方向に冷媒管路20を循環する。冷媒は、圧縮機1で圧縮されて高温高圧のガス状となり、室外熱交換器3で凝縮液化した後、電子式膨張弁2で膨張され、減圧されることで低温低圧の二相状態となり、室内熱交換器4で蒸発ガス化して圧縮機1に戻る。室内空気は、室内熱交換器4を通過する際、低温の冷媒と熱交換を行って低温の空気となり室内に供給される。 The compressor 1, the outdoor heat exchanger 3, the electronic expansion valve 2, and the indoor heat exchanger 4 are connected by a refrigerant pipe line 20 through which a refrigerant flows, and form a refrigerant circuit in which the refrigerant circulates. During the cooling operation, the refrigerant circulates in the refrigerant pipeline 20 in the direction indicated by the solid arrow in FIG. The refrigerant is compressed in the compressor 1 into a high-temperature and high-pressure gaseous state, condensed and liquefied in the outdoor heat exchanger 3, expanded in the electronic expansion valve 2, and decompressed into a low-temperature low-pressure two-phase state, The indoor heat exchanger 4 evaporates and gasifies and returns to the compressor 1. When the indoor air passes through the indoor heat exchanger 4, it exchanges heat with a low-temperature refrigerant to become low-temperature air and is supplied to the room.

冷媒管路20のうち、圧縮機1、室外熱交換器3および電子式膨張弁2を接続する管路を、圧縮機1から流出した高圧冷媒が流通する高圧冷媒管路26とする。また、電子式膨張弁2、室内熱交換器4および圧縮機1を接続する管路を、高圧冷媒管路26よりも低圧の冷媒が流通する低圧冷媒管路25とする。
高圧冷媒管路26には、圧縮機1から吐出された高圧冷媒の一部が流入する高圧制御冷媒通路21が接続されている。一方、低圧冷媒管路25には、圧縮機1に吸入される低圧冷媒の一部が流入する低圧制御冷媒通路22が接続されている。高圧制御冷媒通路21および低圧制御冷媒通路22は、容量制御機構60に連通する制御圧力導入管23に接続されている。
In the refrigerant line 20, the line connecting the compressor 1, the outdoor heat exchanger 3 and the electronic expansion valve 2 is a high-pressure refrigerant line 26 through which the high-pressure refrigerant flowing out of the compressor 1 flows. Further, the pipeline connecting the electronic expansion valve 2, the indoor heat exchanger 4 and the compressor 1 is a low pressure refrigerant pipeline 25 through which a refrigerant having a lower pressure than the high pressure refrigerant pipeline 26 flows.
A high pressure control refrigerant passage 21 into which a part of the high pressure refrigerant discharged from the compressor 1 flows is connected to the high pressure refrigerant pipe line 26. On the other hand, the low-pressure refrigerant conduit 25 is connected to the low-pressure control refrigerant passage 22 into which a part of the low-pressure refrigerant drawn into the compressor 1 flows. The high pressure control refrigerant passage 21 and the low pressure control refrigerant passage 22 are connected to a control pressure introducing pipe 23 that communicates with the capacity control mechanism 60.

高圧制御冷媒通路21には高圧制御弁8が設けられ、低圧制御冷媒通路22には低圧制御弁9が設けられている。高圧制御弁8および低圧制御弁9は、いずれも冷媒の流通/非流通を切り換え可能な電磁弁からなる。
高圧制御弁8と低圧制御弁9は、いずれも制御装置7に接続されており、その開閉は、制御装置7からの指令に基づいて行われる。制御装置7は、高圧制御弁8または低圧制御弁9のうち、いずれか一方を開弁させ、他方を閉弁させる。高圧制御弁8を閉弁させ低圧制御弁9が開弁させた場合は、制御圧力導入管23に低圧冷媒管路25を流通する低圧冷媒の一部が流入する。一方、高圧制御弁8を開弁させ低圧制御弁9が閉弁させた場合は、制御圧力導入管23に高圧冷媒管路26を流通する高圧冷媒の一部が流入する。
The high pressure control refrigerant passage 21 is provided with a high pressure control valve 8, and the low pressure control refrigerant passage 22 is provided with a low pressure control valve 9. Each of the high pressure control valve 8 and the low pressure control valve 9 is an electromagnetic valve capable of switching between circulation and non-circulation of the refrigerant.
The high-pressure control valve 8 and the low-pressure control valve 9 are both connected to the control device 7, and their opening and closing are performed based on a command from the control device 7. The controller 7 opens one of the high pressure control valve 8 and the low pressure control valve 9 and closes the other. When the high pressure control valve 8 is closed and the low pressure control valve 9 is opened, a part of the low pressure refrigerant flowing through the low pressure refrigerant conduit 25 flows into the control pressure introducing pipe 23. On the other hand, when the high pressure control valve 8 is opened and the low pressure control valve 9 is closed, a part of the high pressure refrigerant flowing through the high pressure refrigerant conduit 26 flows into the control pressure introduction pipe 23.

次に、図1および図2を参照しながら、本実施の形態にかかる圧縮機1、および圧縮機1が備える容量制御機構60の構成について詳述する。
図2に示すように、圧縮機1は、圧縮機1の外郭を構成する密閉容器50を有する。また、圧縮機1は、密閉容器50の内部に、冷媒を圧縮するための摺動部として、固定渦巻体54が設けられた固定スクロール51と、搖動渦巻体55が設けられた搖動スクロール52とを備える。固定渦巻体54と搖動渦巻体55は互いに噛み合うように組み合わされ、組み合わされた固定渦巻体54と搖動渦巻体55によって複数の圧縮室Pが構成されている。中心部の圧縮室Pは、高圧冷媒管路26に連通する。
Next, the configuration of the compressor 1 according to the present embodiment and the capacity control mechanism 60 included in the compressor 1 will be described in detail with reference to FIGS. 1 and 2.
As shown in FIG. 2, the compressor 1 has a hermetic container 50 that forms the outer shell of the compressor 1. Further, the compressor 1 includes a fixed scroll 51 provided with a fixed scroll 54 as a sliding portion for compressing a refrigerant inside a closed container 50, and a swing scroll 52 provided with a swing scroll 55. Equipped with. The fixed spiral body 54 and the rocking spiral body 55 are combined so as to mesh with each other, and the fixed spiral body 54 and the rocking spiral body 55 thus combined form a plurality of compression chambers P. The compression chamber P at the center communicates with the high pressure refrigerant pipe line 26.

搖動スクロール52は、予め定められた一定の速度で固定スクロール51に対して搖動し、圧縮室Pを外側の低圧圧縮室から内側の高圧圧縮室に向かって次第に縮小させる。低圧冷媒管路25から圧縮室1に流入した冷媒は、図2の実線矢印にて示すように、圧縮室Pの外側の低圧圧縮室から圧縮室Pに流入し、搖動スクロール52の搖動に伴って圧縮されながら内側の高圧圧縮室に向かう。その後、吐出路53を通じて高圧冷媒管路26に吐出される。 The swing scroll 52 swings with respect to the fixed scroll 51 at a predetermined constant speed, and gradually reduces the compression chamber P from the outer low pressure compression chamber to the inner high pressure compression chamber. The refrigerant flowing into the compression chamber 1 from the low-pressure refrigerant pipe 25 flows into the compression chamber P from the low-pressure compression chamber outside the compression chamber P as shown by the solid line arrow in FIG. 2, and is accompanied by the rocking of the rocking scroll 52. While being compressed, it goes to the inner high-pressure compression chamber. Then, it is discharged to the high-pressure refrigerant pipe 26 through the discharge passage 53.

固定スクロール51には、圧縮機1の容量を制御する容量制御機構60が設けられている。容量制御機構60は、制御圧力導入管23から低圧冷媒または高圧冷媒のいずれか一方が流入する背圧通路61と、バイパス弁64を収容し背圧通路61に連通する背圧室62と、バイパス弁64を弾性支持するコイルスプリング63と、固定スクロール51に設けられ、圧縮途中過程の中間圧縮室の冷媒を低圧空間に戻すバイパス通路65とを含んで構成される。この中間圧縮室はバイパス通路65の形成位置により任意に決定される。低圧空間は、圧縮機1の内部空間のうち、中間圧縮室より低圧の冷媒が存在する任意の空間である。圧縮室Pの外部であってもよいし、中間圧縮室よりも外側の低圧圧縮室であってもよい。なお、本実施の形態では、コイルスプリング63でバイパス弁64を弾性支持する例を示しているが、例えばゴム部材など、他の弾性体で代替してもよい。 The fixed scroll 51 is provided with a capacity control mechanism 60 that controls the capacity of the compressor 1. The capacity control mechanism 60 includes a back pressure passage 61 into which either the low pressure refrigerant or the high pressure refrigerant flows from the control pressure introduction pipe 23, a back pressure chamber 62 that accommodates a bypass valve 64 and communicates with the back pressure passage 61, and a bypass. A coil spring 63 that elastically supports the valve 64 and a bypass passage 65 that is provided in the fixed scroll 51 and that returns the refrigerant in the intermediate compression chamber in the process of compression to the low pressure space are configured. This intermediate compression chamber is arbitrarily determined by the position where the bypass passage 65 is formed. The low-pressure space is an arbitrary space in the internal space of the compressor 1 in which a refrigerant having a lower pressure than the intermediate compression chamber exists. It may be outside the compression chamber P or may be a low pressure compression chamber outside the intermediate compression chamber. In the present embodiment, the coil spring 63 elastically supports the bypass valve 64, but another elastic body such as a rubber member may be used instead.

上述したバイパス弁64には、制御圧力導入管23内の冷媒圧力と中間圧縮室の冷媒圧力とが作用する。背圧通路61に低圧冷媒が流入すると、制御圧力導入管23の冷媒圧力の方が中間圧縮室の冷媒圧力よりも低くなり、バイパス弁64は開弁する。この場合は、中間圧縮室の冷媒の一部がバイパス通路65を通じて低圧空間に戻される。このように、バイパス弁64が開弁して中間圧縮室の冷媒の一部が低圧空間に戻される運転モードをアンロードモード(UL)とする。 The refrigerant pressure in the control pressure introducing pipe 23 and the refrigerant pressure in the intermediate compression chamber act on the bypass valve 64 described above. When the low-pressure refrigerant flows into the back pressure passage 61, the refrigerant pressure in the control pressure introducing pipe 23 becomes lower than the refrigerant pressure in the intermediate compression chamber, and the bypass valve 64 opens. In this case, a part of the refrigerant in the intermediate compression chamber is returned to the low pressure space through the bypass passage 65. In this way, the operation mode in which the bypass valve 64 is opened and a part of the refrigerant in the intermediate compression chamber is returned to the low pressure space is referred to as an unload mode (UL).

一方、背圧通路61に高圧冷媒が流入すると、制御圧力導入管23の冷媒圧力の方が中間圧縮室の冷媒圧力よりも高くなり、バイパス弁64は閉弁する。この場合は、中間圧縮室の冷媒は全て高圧圧縮室に移送され圧縮された後、吐出路53に吐出される。このように、バイパス弁64が閉弁して中間圧縮室の冷媒が全て吐出路53に吐出される運転モードをフルロードモード(FL)とする。 On the other hand, when the high pressure refrigerant flows into the back pressure passage 61, the refrigerant pressure in the control pressure introducing pipe 23 becomes higher than the refrigerant pressure in the intermediate compression chamber, and the bypass valve 64 closes. In this case, all the refrigerant in the intermediate compression chamber is transferred to the high pressure compression chamber, compressed, and then discharged to the discharge passage 53. In this way, the operation mode in which the bypass valve 64 is closed and all the refrigerant in the intermediate compression chamber is discharged to the discharge passage 53 is set to the full load mode (FL).

図1に戻り、説明を続ける。低圧冷媒管路25には、圧縮機1に吸入される冷媒の冷媒温度Tmを検出する冷媒温度センサ11と冷媒圧力Pmを検出する冷媒圧力センサ12(特許請求の範囲における圧力検出手段)が設けられている。冷媒温度センサ11、冷媒圧力センサ12、高圧制御弁8、低圧制御弁9、電子式膨張弁2、室温センサ14およびリモコン15は制御装置7に接続されている。 Returning to FIG. 1, the description will be continued. The low-pressure refrigerant pipe 25 is provided with a refrigerant temperature sensor 11 for detecting the refrigerant temperature Tm of the refrigerant sucked into the compressor 1 and a refrigerant pressure sensor 12 (pressure detecting means in claims) for detecting the refrigerant pressure Pm. Has been. The refrigerant temperature sensor 11, the refrigerant pressure sensor 12, the high pressure control valve 8, the low pressure control valve 9, the electronic expansion valve 2, the room temperature sensor 14, and the remote controller 15 are connected to the control device 7.

制御装置7は、図示しないCPU、ROM、RAM等を備え、空気調和装置10を駆動するための各種プログラムや、関数および固定データ等を記憶している。この制御装置7は、これら関数およびデータ、および各種センサから入力されたデータ等を用いて、各種プログラムを実行し、高圧制御弁8および低圧制御弁9の開閉駆動、電子式膨張弁2の開度調整、およびその他空気調和装置10の駆動処理を実施する。 The control device 7 includes a CPU, a ROM, a RAM, and the like (not shown), and stores various programs for driving the air conditioning apparatus 10, functions, fixed data, and the like. The control device 7 executes various programs by using these functions and data, data input from various sensors, and the like, opens and closes the high pressure control valve 8 and the low pressure control valve 9, and opens the electronic expansion valve 2. The degree adjustment and other drive processing of the air conditioning apparatus 10 are performed.

例えば、制御装置7は、冷媒温度センサ11によって検出された冷媒温度Tmと冷媒圧力センサ12によって検出された冷媒圧力Pmから、圧縮機1に流入する冷媒の過熱度SH1を算出し、この算出した過熱度SH1に基づいて電子式膨張弁2の開度を調整する。 For example, the control device 7 calculates the superheat degree SH1 of the refrigerant flowing into the compressor 1 from the refrigerant temperature Tm detected by the refrigerant temperature sensor 11 and the refrigerant pressure Pm detected by the refrigerant pressure sensor 12, and this calculation is performed. The opening degree of the electronic expansion valve 2 is adjusted based on the superheat degree SH1.

制御装置7は、算出した過熱度SH1と予め記憶している閾値SHTとを比較し、過熱度SH1と閾値SHTとの差に応じて電子式膨張弁2の開度を調整する。過熱度SH1が閾値SHTよりも大きい場合は過熱度SH1と閾値SHTとの差が大きいほど電子式膨張弁2の開度を大きくして、過熱度SH1を小さくする。過熱度SH1が閾値SHTよりも小さい場合は、過熱度SH1と閾値SHTとの差が大きいほど電子式膨張弁2の開度を小さくして、過熱度SH1を大きくする。SH1が閾値SHTと等しい場合は、電子式膨張弁2の開度は変更しない。閾値SHTは、一般に、5〜10℃に設定されるが、この限りではない。 The control device 7 compares the calculated superheat degree SH1 with a threshold value SHT stored in advance, and adjusts the opening degree of the electronic expansion valve 2 according to the difference between the superheat degree SH1 and the threshold value SHT. When the superheat degree SH1 is larger than the threshold value SHT, the larger the difference between the superheat degree SH1 and the threshold value SHT, the larger the opening degree of the electronic expansion valve 2 and the smaller the superheat degree SH1. When the superheat degree SH1 is smaller than the threshold value SHT, the larger the difference between the superheat degree SH1 and the threshold value SHT, the smaller the opening degree of the electronic expansion valve 2 and the larger the superheat degree SH1. When SH1 is equal to the threshold value SHT, the opening degree of the electronic expansion valve 2 is not changed. The threshold SHT is generally set to 5 to 10°C, but is not limited to this.

また、制御装置7は、以下の式(1)を用いて、室温センサ14の検出温度Trとユーザがリモコン15を通じて設定した設定温度Toとの偏差ΔTを算出し、この偏差ΔTに基づいて圧縮機1の運転モードを決定する。

ΔT=Tr−To・・・(1)
Further, the control device 7 calculates the deviation ΔT between the detected temperature Tr of the room temperature sensor 14 and the set temperature To set by the user through the remote controller 15 using the following equation (1), and compresses based on this deviation ΔT. Determine the operating mode of machine 1.

ΔT=Tr−To (1)

制御装置7は、偏差ΔTの上限値Tuと下限値Tlを記憶しており、偏差ΔTが上限値Tu以上であると判断した場合はフルロードモードで圧縮機1を駆動する。一方、偏差ΔTが下限値Tl未満である場合と判断した場合は、アンロードモードで圧縮機1を駆動する。これに対して、偏差ΔTが下限値Tl以上であり且つ上限値Tu未満である場合は、運転モードの切り換えを行わず、現状の運転モードで空気調和装置10を駆動する。 The control device 7 stores the upper limit value Tu and the lower limit value Tl of the deviation ΔT, and drives the compressor 1 in the full load mode when it determines that the deviation ΔT is equal to or larger than the upper limit value Tu. On the other hand, when it is determined that the deviation ΔT is less than the lower limit value Tl, the compressor 1 is driven in the unload mode. On the other hand, when the deviation ΔT is greater than or equal to the lower limit value Tl and less than the upper limit value Tu, the operation mode is not switched and the air conditioner 10 is driven in the current operation mode.

ところで、運転モードをフルロードモードからアンロードモードに切り換えるためにバイパス弁64を閉弁状態から開弁状態に切り換えると、圧縮機1からの冷媒排出量が急減するため、低圧冷媒管路25の冷媒流通量が一時的に急増する。冷媒温度センサ11および冷媒圧力センサ12には過熱度SH1を精度よく検出することを目的としてある程度大きい時定数が設定されているため、運転モードの変更に伴う冷媒流通量の変化の影響が過熱度SH1の変動として現れるまでには、時間的なずれが発生する。このような時間的なずれが発生すると、冷媒流通量の変化が過熱度SH1の変動として検出される前に低圧冷媒管路25の冷媒流通量が室内熱交換器4の熱交換能力を超えて増加し、一部の冷媒が蒸発せずに圧縮機1に流入するいわゆる液バックが発生する恐れがある。 By the way, when the bypass valve 64 is switched from the closed state to the open state in order to switch the operation mode from the full load mode to the unload mode, the refrigerant discharge amount from the compressor 1 is rapidly reduced. The flow rate of refrigerant temporarily increases rapidly. Since the refrigerant temperature sensor 11 and the refrigerant pressure sensor 12 are set to have a relatively large time constant for the purpose of accurately detecting the superheat degree SH1, the influence of the change in the refrigerant flow amount due to the change of the operation mode is influenced by the superheat degree. There is a time lag until it appears as a change in SH1. When such a time lag occurs, the refrigerant flow amount of the low-pressure refrigerant pipe 25 exceeds the heat exchange capacity of the indoor heat exchanger 4 before the change of the refrigerant flow amount is detected as the change of the superheat degree SH1. There is a possibility that a so-called liquid bag may be generated in which a part of the refrigerant increases and flows into the compressor 1 without evaporating.

そこで、本実施の形態では、圧縮機1の運転モードがフルロードモードからアンロードモードに切り換られたことに基づき、すなわちバイパス弁64が閉弁状態から開弁状態に切り換えられたことに基づき、制御装置7は、電子式膨張弁2の開度を過熱度SH1に基づいて設定される開度よりも所定開度θaだけ小さい開度に減算補正する制限処理を開始する。なお、所定開度θaは、バイパス弁64を閉弁状態から開弁状態に切り換えることによる冷媒流通量の増加を抑制するために必要な開度であり、任意に設定される。所定開度θa減算補正した後の電子式制御弁2の開度が、室内熱交換器4の熱交換能力の下限に相当する量の冷媒を通過させる開度となる値に設定されることが好ましいが、この限りではない。但し、所定開度θaが大きすぎると、圧縮機1内の冷媒圧力が急減し固定渦巻体54と搖動渦巻体55が冷媒を介さず直接に接触摺動し、焼き付き等の不具合が発生するおそれがある。このため、所定開度θaは、圧縮機1内の冷媒量を加味して設定されることがより好ましい。 Therefore, in the present embodiment, the operation mode of the compressor 1 is switched from the full load mode to the unload mode, that is, the bypass valve 64 is switched from the closed state to the open state. The control device 7 starts the limiting process of subtracting and correcting the opening degree of the electronic expansion valve 2 to the opening degree smaller than the opening degree set based on the superheat degree SH1 by the predetermined opening degree θa. It should be noted that the predetermined opening degree θa is an opening degree required to suppress an increase in the refrigerant flow amount due to switching the bypass valve 64 from the closed state to the open state, and is set arbitrarily. The opening of the electronic control valve 2 after the subtraction correction by the predetermined opening θa may be set to a value that allows the amount of refrigerant to pass through which corresponds to the lower limit of the heat exchange capacity of the indoor heat exchanger 4. Preferred, but not limited to this. However, if the predetermined opening degree θa is too large, the pressure of the refrigerant in the compressor 1 is suddenly reduced, and the fixed spiral body 54 and the swinging spiral body 55 may come into direct contact sliding with each other without interposing the refrigerant, and a problem such as seizure may occur. There is. Therefore, the predetermined opening degree θa is more preferably set in consideration of the amount of refrigerant in the compressor 1.

これに対して、運転モードをアンロードモードからフルロードモードに切り換えるため、バイパス弁64を開弁状態から閉弁状態に切り換えると、圧縮機1の冷媒吸入量は変化しないにも関わらず、圧縮機1からの冷媒排出量は一時的に急増するため、圧縮機1内の冷媒量は一時的に急減する。圧縮機1内の冷媒量が急減すると、固定渦巻体54と搖動渦巻体55とが冷媒を介さず直接に接触摺動し、焼き付き等の不具合が発生するおそれがある。 On the other hand, in order to switch the operation mode from the unload mode to the full load mode, when the bypass valve 64 is switched from the open state to the closed state, the refrigerant suction amount of the compressor 1 does not change, but the compression amount is reduced. Since the refrigerant discharge amount from the machine 1 temporarily increases rapidly, the refrigerant amount in the compressor 1 temporarily decreases rapidly. If the amount of the refrigerant in the compressor 1 is suddenly reduced, the fixed spiral body 54 and the swinging spiral body 55 may directly contact and slide with each other without using the refrigerant, and a problem such as seizure may occur.

そこで、制御装置7は、アンロードモードからフルロードモードに切り換える要求を検出した場合、すなわち運転モードがアンロードモードにあるときに偏差ΔTが上限値Tu以上となったことを検出した場合は、電子式膨張弁2の開度を過熱度SH1に基づいて設定される開度に対して所定開度θbを加算補正する促進処理を実施した後、圧縮機1の運転モードをフルロードモードに切り換える。なお、所定開度θbは、バイパス弁64を開弁状態から閉弁状態に切り換えることによる圧縮機1内の冷媒量の急減を抑制するために必要な開度であり、任意に設定される。例えば、所定開度θb加算補正した後の電子式制御弁2の開度が、室内熱交換器4の熱交換能力の上限に相当する量の冷媒を通過させる開度となる値に設定されることが好ましいが、この限りではない。 Therefore, when the control device 7 detects a request to switch from the unload mode to the full load mode, that is, when the deviation ΔT becomes equal to or larger than the upper limit value Tu when the operation mode is the unload mode, After performing an acceleration process of correcting the opening degree of the electronic expansion valve 2 by adding the predetermined opening degree θb to the opening degree set based on the superheat degree SH1, the operation mode of the compressor 1 is switched to the full load mode. .. The predetermined opening degree θb is an opening degree necessary for suppressing a sharp decrease in the amount of refrigerant in the compressor 1 caused by switching the bypass valve 64 from the open state to the closed state, and is set arbitrarily. For example, the opening degree of the electronic control valve 2 after the addition and correction of the predetermined opening degree θb is set to a value that allows the refrigerant to pass through an amount corresponding to the upper limit of the heat exchange capacity of the indoor heat exchanger 4. However, it is not limited to this.

次に、図3のフローチャートを参照しながら、本実施の形態における空気調和装置10の動作について説明する。なお、制御装置7は、同図3のフローチャートと並行して、冷媒温度センサ11で検出される冷媒温度Tmと冷媒圧力センサ12で検出される冷媒圧力Pmに基づいて過熱度SH1を算出し、この過熱度SH1に基づいて適切な電子式膨張弁2の開度を常時算出するものとする。
まず、ユーザがリモコン15を操作して空気調和装置10のオン制御を実行すると、圧縮機1が駆動を開始する。圧縮機1が駆動されることで、空気調和装置10による運転が開始される。
制御装置7は、圧縮機1の駆動が開始されると、まず、上記式(1)に基づいて、室温センサ14の検出温度Trとユーザが入力した設定温度Toとの偏差(ΔT)を算出する(ステップS10)。
Next, the operation of the air conditioner 10 in the present embodiment will be described with reference to the flowchart in FIG. Note that the control device 7 calculates the superheat degree SH1 based on the refrigerant temperature Tm detected by the refrigerant temperature sensor 11 and the refrigerant pressure Pm detected by the refrigerant pressure sensor 12, in parallel with the flowchart of FIG. It is assumed that the appropriate opening degree of the electronic expansion valve 2 is constantly calculated based on the superheat degree SH1.
First, when the user operates the remote controller 15 to execute ON control of the air conditioning apparatus 10, the compressor 1 starts driving. By driving the compressor 1, the operation by the air conditioner 10 is started.
When the drive of the compressor 1 is started, the control device 7 first calculates the deviation (ΔT) between the detected temperature Tr of the room temperature sensor 14 and the set temperature To input by the user based on the above equation (1). (Step S10).

次に、制御装置7は、算出した偏差ΔTが、予め記憶している上限値Tu以上であるか否かを判断する(ステップS11)。偏差ΔTが上限値Tu未満であると判断する場合(ステップS11;NO)、偏差ΔTが下限値Tl未満であるか否かを判断する(ステップS12)。
偏差ΔTが下限値Tl未満でないと判断する場合(ステップS12;NO)、すなわち偏差ΔTが上限値Tu未満且つ下限値Tl以上であると判断する場合は、圧縮機1の運転モードの変更は行わない。この場合、制御装置7は、電子式膨張弁2の開度補正を実施しない。
Next, the control device 7 determines whether the calculated deviation ΔT is equal to or larger than the upper limit value Tu stored in advance (step S11). When it is determined that the deviation ΔT is less than the upper limit value Tu (step S11; NO), it is determined whether the deviation ΔT is less than the lower limit value Tl (step S12).
When it is determined that the deviation ΔT is not less than the lower limit value Tl (step S12; NO), that is, when the deviation ΔT is less than the upper limit value Tu and not less than the lower limit value Tl, the operation mode of the compressor 1 is changed. Absent. In this case, the control device 7 does not perform the opening degree correction of the electronic expansion valve 2.

一方、偏差ΔTが下限値Tl未満であると判断する場合(ステップS12;YES)、制御装置7は、圧縮機1の運転モードをアンロードモードに切り換える。まず、制御装置7は、圧縮機1の運転モードがフルロードモードにあるか否かを判断する(ステップS13)。 On the other hand, when determining that the deviation ΔT is less than the lower limit value Tl (step S12; YES), the control device 7 switches the operation mode of the compressor 1 to the unload mode. First, the control device 7 determines whether the operation mode of the compressor 1 is the full load mode (step S13).

本実施の形態では、低圧制御弁9が開弁し高圧制御弁8が閉弁している場合、バイパス弁64が開弁状態にあることとなるため、圧縮機1はアンロードモードにあると判断する。一方、低圧制御弁9が閉弁し高圧制御弁8が開弁している場合、バイパス弁64が閉弁状態にあることとなるため、圧縮機1はフルロードモードにあると判断する。なお、本実施の形態では、圧縮機1がアンロードモードまたはフルロードモードのいずれにあるかの判断は、低圧制御弁9または高圧制御弁8のいずれが開弁状態にあるかを判断することにより行うが、圧縮機1の運転モードの判断は、他の公知の方法を用いて行うこともできる。例えば、制御圧力導入管23の冷媒圧力Pmに基づいて判断してもよいし、バイパス弁64の開閉を感知するセンサを用いてもよいが、これらの方法に限られるものではなく、公知の他の方法を用いることができる。 In the present embodiment, when the low pressure control valve 9 is open and the high pressure control valve 8 is closed, the bypass valve 64 is in the open state, so that the compressor 1 is in the unload mode. to decide. On the other hand, when the low-pressure control valve 9 is closed and the high-pressure control valve 8 is open, the bypass valve 64 is in the closed state, so the compressor 1 is determined to be in the full load mode. In this embodiment, whether the compressor 1 is in the unload mode or the full load mode is determined by determining which of the low pressure control valve 9 and the high pressure control valve 8 is open. However, the determination of the operation mode of the compressor 1 can also be performed by using another known method. For example, the determination may be made based on the refrigerant pressure Pm of the control pressure introducing pipe 23, or a sensor that detects the opening/closing of the bypass valve 64 may be used, but the method is not limited to these methods, and other known methods may be used. Can be used.

圧縮機1の運転モードがフルロードモードにないと判断する場合(ステップS13;NO)、すなわち圧縮機1がアンロードモードにあると判断する場合は、運転モードの変更を行わず、電子式膨張弁2の開度補正も実施しない。 When it is determined that the operation mode of the compressor 1 is not the full load mode (step S13; NO), that is, when the compressor 1 is in the unload mode, the operation mode is not changed and the electronic expansion is performed. The opening degree of the valve 2 is not corrected.

一方、圧縮機1の運転モードがフルロードモードにあると判断する場合(ステップS13;YES)、制御装置7は、圧縮機1の運転モードをアンロードモードに切り換え(ステップS14)、制限処理を開始する(ステップS15)。制限処理が開始されると、制御装置7は、過熱度SH1に基づいて算出した電子式膨張弁2の開度に対して、上述した所定開度θa減算する開度補正を行い、電子式膨張弁2の開度を補正後の開度に設定する。 On the other hand, when determining that the operation mode of the compressor 1 is the full load mode (step S13; YES), the control device 7 switches the operation mode of the compressor 1 to the unload mode (step S14), and performs the limiting process. Start (step S15). When the restriction process is started, the control device 7 performs the opening correction by subtracting the above-described predetermined opening θa from the opening of the electronic expansion valve 2 calculated based on the superheat degree SH1 to perform the electronic expansion. The opening of the valve 2 is set to the corrected opening.

次に、制御装置7は、制限処理を開始してからの経過期間Taが所定期間T1以上であるか否かを判断する(ステップS16)。所定期間T1は、冷媒圧力Pmが低下するのに十分な期間であり任意に設定される。例えば、中間圧縮室から低圧空間に戻される冷媒量に相当する量の冷媒が電子式制御弁2を通過するのに必要な期間が好ましいが、この限りではない。 Next, the control device 7 determines whether the elapsed period Ta from the start of the limiting process is the predetermined period T1 or more (step S16). The predetermined period T1 is a period sufficient for the refrigerant pressure Pm to decrease, and is set arbitrarily. For example, the period required for the amount of refrigerant corresponding to the amount of the refrigerant returned from the intermediate compression chamber to the low pressure space to pass through the electronic control valve 2 is preferable, but it is not limited to this.

経過期間Taが所定期間T1未満であると判断する場合(ステップS16;NO)は制限処理を継続し、経過期間Taが所定期間T1以上であると判断する場合(ステップS16;YES)、制限処理を終了する(ステップS17)。すなわち、電子式膨張弁2の開度補正を終了する。 When it is determined that the elapsed period Ta is less than the predetermined period T1 (step S16; NO), the limiting process is continued, and when it is determined that the elapsed period Ta is equal to or more than the predetermined period T1 (step S16; YES), the limiting process is performed. Is finished (step S17). That is, the opening degree correction of the electronic expansion valve 2 is completed.

これに対して、偏差ΔTが上限値Tu以上であると判断する場合(ステップS11;YES)、上述した方法で、圧縮機1がアンロードモードにあるか否かを判断する(ステップS18)。 On the other hand, when it is determined that the deviation ΔT is equal to or greater than the upper limit value Tu (step S11; YES), it is determined whether the compressor 1 is in the unload mode by the method described above (step S18).

圧縮機1がアンロードモードにあると判断する場合(ステップS18;YES)、制御装置7は、偏差ΔTが上限値Tu以上であり、且つ運転モードがアンロードモードにあることから、運転モードをアンロードモードからフルロードモードに切り換える切り換え要求があると判断する。 When it is determined that the compressor 1 is in the unload mode (step S18; YES), the control device 7 determines that the deviation ΔT is equal to or larger than the upper limit value Tu and the operation mode is in the unload mode. It is determined that there is a switching request to switch from unload mode to full load mode.

この際、制御装置7は、運転モードをフルロードモードに切り換えるのに先立って、促進処理を開始する(ステップS19)。促進処理が開始されると、制御装置7は、過熱度SH1に基づいて算出した電子式膨張弁2の開度に対して、上述した所定開度θbを加算する開度補正を行い、電子式膨張弁2の開度を補正後の開度に設定する。 At this time, the control device 7 starts the acceleration process before switching the operation mode to the full load mode (step S19). When the acceleration process is started, the control device 7 performs an opening degree correction to add the above-described predetermined opening degree θb to the opening degree of the electronic expansion valve 2 calculated based on the superheat degree SH1, The opening of the expansion valve 2 is set to the corrected opening.

次に、制御装置7は、促進処理を開始してからの経過期間Tbが所定期間T2以上であるか否かを判断する(ステップS20)。所定期間T2は、運転モードの変更に伴って圧縮機1からの冷媒吐出量が急増しても、圧縮機1内に不具合が発生しない量の冷媒を圧縮機1内に確保するのに必要な期間であり、任意に設定される。例えば、中間圧縮室から低圧空間に戻される冷媒量に相当する量の冷媒が圧縮室1に貯留されるのに必要な期間が好ましいが、この限りではない。 Next, the control device 7 determines whether or not the elapsed period Tb from the start of the promotion process is the predetermined period T2 or more (step S20). The predetermined time period T2 is necessary to secure a sufficient amount of refrigerant in the compressor 1 that does not cause a problem in the compressor 1 even if the refrigerant discharge amount from the compressor 1 rapidly increases due to a change in the operation mode. The period, which is set arbitrarily. For example, it is preferable that the period required to store the refrigerant in the compression chamber 1 in an amount corresponding to the amount of the refrigerant returned from the intermediate compression chamber to the low pressure space is not limited to this.

経過期間Tbが所定期間T2未満であると判断する場合(ステップS20;NO)は促進処理を継続し、経過期間Tbが所定期間T2以上であると判断する場合(ステップS20;YES)、促進処理を終了する(ステップS21)。すなわち、電子式膨張弁2の開度補正を終了する。また、圧縮機1の運転モードをフルロードモードに切り換える(ステップS21)。 When it is determined that the elapsed period Tb is less than the predetermined period T2 (step S20; NO), the promotion process is continued, and when it is determined that the elapsed period Tb is equal to or greater than the predetermined period T2 (step S20; YES), the promotion process. Is finished (step S21). That is, the opening degree correction of the electronic expansion valve 2 is completed. Further, the operation mode of the compressor 1 is switched to the full load mode (step S21).

一方、圧縮機1がアンロードモードにないと判断する場合(ステップS18;NO)、すなわち、圧縮機1がフルロードモードにあると判断する場合、圧縮機1の運転モードの変更は行わない。この場合、制御装置7は、電子式膨張弁2の開度補正は実施しない。
次に、制御装置7は、空気調和装置10の運転が終了したか否かを判断する(ステップS22)。制御装置7は、空気調和装置10の運転が終了したと判断する場合(ステップS22;YES)、この処理を終了し、空気調和装置10の運転が継続していると判断する場合(ステップS22;NO)、ステップS10に戻ってこの処理を継続する。
On the other hand, when it is determined that the compressor 1 is not in the unload mode (step S18; NO), that is, when the compressor 1 is in the full load mode, the operation mode of the compressor 1 is not changed. In this case, the controller 7 does not correct the opening degree of the electronic expansion valve 2.
Next, the control device 7 determines whether or not the operation of the air conditioner 10 has ended (step S22). When determining that the operation of the air conditioner 10 has ended (step S22; YES), the control device 7 ends this processing and determines that the operation of the air conditioner 10 is continuing (step S22; NO), and returns to step S10 to continue this process.

図4に、図3にて説明した処理を行った場合の(a)電子式膨張弁2の開度、(b)室温センサ14の検出温度Trおよび設定温度To、(c)冷媒圧力センサ12で検出した冷媒圧力Pm、(d)圧縮機1の運転モードの各推移についてその一例を示す。 4, (a) the opening degree of the electronic expansion valve 2, (b) the detected temperature Tr and the set temperature To of the room temperature sensor 14, and (c) the refrigerant pressure sensor 12 when the processing described in FIG. 3 is performed. One example of each transition of the refrigerant pressure Pm detected in step (d) and the operation mode of the compressor (d) will be shown.

図4(a)には、上述した制限処理および促進処理を実施した場合における電子式膨張弁2の開度の推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における電子式膨張弁2の開度の推移の一例を二点鎖線にて示している。図4(b)には、ユーザがリモコン15を通じて設定した設定温度Toの推移の一例を実線にて示し、室温センサ14による検出温度Trの推移の一例を一点鎖線にて示す。図4(c)には、上述した制限処理および促進処理を実施した場合における冷媒圧力Pmの推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における冷媒圧力Pmの推移の一例を二点鎖線にて示している。図4(d)には、上述した制限処理および促進処理を実施した場合における圧縮機1の運転モードの推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における圧縮機1の運転モードの推移の一例を二点鎖線にて示している。 In FIG. 4A, a solid line shows an example of the transition of the opening degree of the electronic expansion valve 2 when the restriction process and the acceleration process described above are performed, and in the case where the restriction process and the acceleration process described above are not performed. An example of transition of the opening degree of the electronic expansion valve 2 is shown by a two-dot chain line. In FIG. 4B, an example of the transition of the set temperature To set by the user through the remote controller 15 is shown by a solid line, and an example of the transition of the temperature Tr detected by the room temperature sensor 14 is shown by a dashed line. In FIG. 4(c), an example of the transition of the refrigerant pressure Pm in the case where the above-mentioned restriction process and promotion process are performed is shown by a solid line, and the transition of the refrigerant pressure Pm in the case where the above-mentioned restriction process and promotion process are not performed An example is shown by a chain double-dashed line. In FIG. 4D, a solid line shows an example of the transition of the operation mode of the compressor 1 when the above-described restriction processing and acceleration processing are performed, and the compressor when the above-described restriction processing and acceleration processing is not performed. An example of transition of the operation mode of No. 1 is shown by a two-dot chain line.

同図4に示すように、設定温度Toと検出温度Trとの偏差ΔTが上限値Tu以上であると、圧縮機1はフルロードモードで運転される(タイミングt0〜t1)。 As shown in FIG. 4, when the deviation ΔT between the set temperature To and the detected temperature Tr is not less than the upper limit value Tu, the compressor 1 is operated in the full load mode (timing t0 to t1).

偏差ΔTが上限値Tu未満となった後、さらに下限値Tl未満となると、制御装置7は、圧縮機1の運転モードをフルロードモードからアンロードモードに切り換える。この際、制御装置7は、過熱度SH1に基づいて算出される電子式膨張弁2の開度に対して所定角度θaを減算する制限処理を開始する(タイミングt1)。この制限処理は、所定期間T1に渡って継続する(タイミングt1〜t2)。 When the deviation ΔT becomes smaller than the upper limit value Tu and further becomes smaller than the lower limit value Tl, the control device 7 switches the operation mode of the compressor 1 from the full load mode to the unload mode. At this time, the control device 7 starts the limiting process of subtracting the predetermined angle θa from the opening degree of the electronic expansion valve 2 calculated based on the superheat degree SH1 (timing t1). This restriction process continues for a predetermined period T1 (timing t1 to t2).

制限処理が実施されると、電子式膨張弁2の開度が低下することに伴い、低圧冷媒管路25を流通する冷媒量が低下するため、冷媒圧力Pmの一時的な上昇が抑制される。所定期間T1が経過すると、制御装置7は、制限処理を終了する(タイミングt2)。 When the limiting process is performed, the opening amount of the electronic expansion valve 2 decreases and the amount of the refrigerant flowing through the low-pressure refrigerant pipe 25 decreases, so that the temporary increase in the refrigerant pressure Pm is suppressed. .. When the predetermined period T1 has elapsed, the control device 7 ends the limiting process (timing t2).

その後、設定温度Toが変更され、偏差ΔTが上限値Tu以上になると(タイミングt3)、制御装置7は、運転モードの切り換え要求があると判断する。
この場合、制御装置7は、運転モードをアンロードモードからフルロードモードに切り換えるに先立って、電子式膨張弁2の開度を過熱度SH1から算出される開度に対して所定開度θbを加算補正する促進処理を開始する(タイミングt3)。この促進処理は、所定期間T2に渡って継続する(タイミングt3〜t4)。この間、運転モードはアンロードモードに維持する。
After that, when the set temperature To is changed and the deviation ΔT becomes equal to or larger than the upper limit value Tu (timing t3), the control device 7 determines that there is a request for switching the operation mode.
In this case, the control device 7 sets the opening degree of the electronic expansion valve 2 to the predetermined opening degree θb with respect to the opening degree calculated from the superheat degree SH1 before switching the operation mode from the unload mode to the full load mode. A promotion process for addition correction is started (timing t3). This promotion process continues for a predetermined period T2 (timing t3 to t4). During this time, the operation mode is maintained in the unload mode.

促進処理が実施されると、電子式膨張弁2の開度の増加に伴い、低圧冷媒管路25を流通する冷媒量が増加するため、冷媒圧力Pmが増加する(タイミングt3〜t4)。所定期間T2が経過すると、制御装置7は、促進処理を終了する(タイミングt4)。すなわち、制御装置7は、電子式膨張弁2の開度補正を終了する。また、制御装置7は、圧縮機1の運転モードをアンロードモードからフルロードモードに切り換える。 When the acceleration process is performed, the amount of the refrigerant flowing through the low-pressure refrigerant pipe line 25 increases as the opening degree of the electronic expansion valve 2 increases, so that the refrigerant pressure Pm increases (timing t3 to t4). When the predetermined period T2 has elapsed, the control device 7 ends the promotion process (timing t4). That is, the control device 7 ends the opening degree correction of the electronic expansion valve 2. Further, the control device 7 switches the operation mode of the compressor 1 from the unload mode to the full load mode.

上述した実施の形態1によれば、以下に示す効果を奏することができる。 According to the above described first embodiment, the following effects can be obtained.

・バイパス弁64を閉弁状態から開弁状態に切り換えたことに基づいて、電子式膨張弁2の開度に所定開度θaを減算補正する制限処理を開始するため、圧縮機1の容量の変化が過熱度SH1の変動に反映される前に、冷媒流通量を低下させることができる。このため、圧縮機1の容量を変更することによる液バックの発生を従来よりも抑制することができる。 The capacity of the compressor 1 is reduced to start the limiting process of subtracting the predetermined opening θa from the opening of the electronic expansion valve 2 based on the switching of the bypass valve 64 from the closed state to the open state. The refrigerant flow rate can be reduced before the change is reflected in the change in the superheat degree SH1. Therefore, the occurrence of liquid back due to the change in the capacity of the compressor 1 can be suppressed more than ever before.

・バイパス弁64を開弁状態から閉弁状態に切り換える前に、電子式膨張弁2の開度に所定開度θbを加算補正する促進処理を開始するため、圧縮機1の容量が変化する前に、圧縮機1内に貯留される冷媒量を増加させることができる。このため、圧縮機1内の冷媒量が急減して固定渦巻体54と搖動渦巻体55が冷媒を介さずに直接に接触摺動することを抑制することができる。 Before the bypass valve 64 is switched from the open state to the closed state, the acceleration process of adding and correcting the predetermined opening degree θb to the opening degree of the electronic expansion valve 2 is started, so that the capacity of the compressor 1 is not changed. In addition, the amount of refrigerant stored in the compressor 1 can be increased. Therefore, it is possible to prevent the amount of the refrigerant in the compressor 1 from suddenly decreasing and the fixed spiral body 54 and the swinging spiral body 55 to directly contact and slide without the intermediary of the refrigerant.

・制限処理を所定期間T1に渡って実施するため、ハンチングの発生を抑制し、より好適に液バックの発生を抑制することができる。 Since the limiting process is performed for the predetermined period T1, the occurrence of hunting can be suppressed, and the occurrence of liquid back can be suppressed more preferably.

・促進処理を所定期間T2に渡って実施するため、ハンチングの発生を抑制し、より好適に固定渦巻体54と搖動渦巻体55とが直接に接触摺動することを抑制することができる。 Since the acceleration process is performed for the predetermined period T2, it is possible to suppress the occurrence of hunting and more preferably suppress the direct contact and sliding of the fixed spiral body 54 and the swing spiral body 55.

(実施の形態2)
実施の形態2の空気調和装置10の制御方法について、先の図1〜4の他、更に図5、図6を併せ参照して説明する。なお、特に断りの無い場合、同一符号は同一の構成を示し、実施の形態1と同様の処理については、同一のステップ番号を付すことによりその詳細な説明を適宜割愛する。
(Embodiment 2)
A control method of the air-conditioning apparatus 10 according to the second embodiment will be described with reference to FIGS. 1 to 4 and FIGS. It should be noted that, unless otherwise specified, the same reference numerals indicate the same configurations, and the same processes as those in the first embodiment are denoted by the same step numbers, and the detailed description thereof will be appropriately omitted.

図5は、実施の形態2に係る空気調和装置10の制御フローチャートである。図5を参照して実施の形態2に係る制御装置7の動作について説明する。図5に示す制御フローチャートは、図3のフローチャートのステップS15〜17を、ステップS30〜S34に置き換えたものであり、その他のステップについては同様である。そこで、同様の制御内容については説明を省略する。 FIG. 5 is a control flowchart of the air conditioner 10 according to the second embodiment. The operation of the control device 7 according to the second embodiment will be described with reference to FIG. The control flowchart shown in FIG. 5 is obtained by replacing steps S15 to 17 of the flowchart of FIG. 3 with steps S30 to S34, and the other steps are the same. Therefore, description of similar control contents is omitted.

制御装置7は、圧縮機1の運転モードをアンロードモードに切り換えた(ステップS14)後、冷媒圧力センサ12によって検出される冷媒圧力Pmが閾値P1(特許請求の範囲における第1所定圧力)以上であるか否かを判断する(ステップS30)。閾値P1は、室内熱交換器4の熱交換能力の上限に相当する量の冷媒が通過する場合における冷媒圧力であることが好ましい。 The controller 7 switches the operation mode of the compressor 1 to the unload mode (step S14), and then the refrigerant pressure Pm detected by the refrigerant pressure sensor 12 is equal to or higher than the threshold value P1 (first predetermined pressure in claims). Or not (step S30). The threshold value P1 is preferably the refrigerant pressure when the amount of refrigerant corresponding to the upper limit of the heat exchange capacity of the indoor heat exchanger 4 passes.

制御装置7は、冷媒圧力Pmが閾値P1未満であると判断する場合(ステップS30;NO)、運転モードをアンロードモードに切り換えてからの経過期間Tcが所定期間T3以上である否かを判断する(ステップS31)。所定期間T3は、圧縮機1の運転モードをアンロードモードに切り換えた後、一時的に増加した吸入圧力が定常状態に戻るために必要な期間であり、任意に設定される。中間圧縮室から低圧空間に戻される冷媒量に相当する量の冷媒が電子式制御弁2を通過する期間とすることが好ましいが、この限りではない。 When determining that the refrigerant pressure Pm is less than the threshold value P1 (step S30; NO), the control device 7 determines whether or not the elapsed period Tc after switching the operation mode to the unload mode is the predetermined period T3 or more. Yes (step S31). The predetermined period T3 is a period required to return the temporarily increased suction pressure to the steady state after switching the operation mode of the compressor 1 to the unload mode, and is set arbitrarily. It is preferable to set the period in which the amount of the refrigerant corresponding to the amount of the refrigerant returned from the intermediate compression chamber to the low pressure space passes through the electronic control valve 2, but not limited to this.

アンロードモードに切り換えた後の経過期間Tcが所定期間T3未満であると判断する場合(ステップS31;NO)、ステップS30に戻る。一方、アンロードモードに切り換えてからの経過期間Tcが所定期間T3以上であると判断する場合(ステップS31;YES)、この処理を一旦終了する。 When it is determined that the elapsed period Tc after switching to the unload mode is less than the predetermined period T3 (step S31; NO), the process returns to step S30. On the other hand, when it is determined that the elapsed period Tc after switching to the unload mode is the predetermined period T3 or more (step S31; YES), this process is temporarily terminated.

これに対して、冷媒圧力Pmが閾値P1以上であると判断する場合(ステップS30;YES)、制限処理を開始する(ステップS32)。そして、制限処理開始後の経過期間Taが所定期間T1以上であるか否かを判断し(ステップS33)、制限処理開始後の経過期間Taが所定期間T1以上と判断する場合(ステップS33;NO)、ステップS33に戻り、制限処理開始後の経過期間Taが所定期間1以上と判断する場合(ステップS33;YES)、この制限処理を終了する(ステップS34)。 On the other hand, when it is determined that the refrigerant pressure Pm is equal to or higher than the threshold value P1 (step S30; YES), the limiting process is started (step S32). Then, it is determined whether or not the elapsed period Ta after the start of the limiting process is equal to or longer than the predetermined period T1 (step S33), and it is determined that the elapsed period Ta after the start of the limiting process is equal to or larger than the predetermined period T1 (step S33; NO). ), the process returns to step S33, and when it is determined that the elapsed period Ta after the start of the restriction process is equal to or longer than the predetermined period 1 (step S33; YES), the restriction process ends (step S34).

図6に、図5にて説明した処理を行った場合の(a)電子式膨張弁2の開度、(b)室温センサ14の検出温度Trおよび設定温度To、(c)冷媒圧力センサ12で検出した冷媒圧力Pm、(d)圧縮機1の運転モードの各推移についてその一例を示す。 6, (a) the opening degree of the electronic expansion valve 2, (b) the detected temperature Tr and the set temperature To of the room temperature sensor 14, and (c) the refrigerant pressure sensor 12 when the processing described in FIG. 5 is performed. One example of each transition of the refrigerant pressure Pm detected in step (d) and the operation mode of the compressor (d) will be shown.

図6(a)には、上述した制限処理および促進処理を実施した場合における電子式膨張弁2の開度の推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における電子式膨張弁2の開度の推移の一例を二点鎖線にて示している。図6(b)には、ユーザがリモコン15を通じて設定した設定温度Toの推移の一例を実線にて示し、室温センサ14による検出温度Trの推移の一例を一点鎖線にて示す。図6(c)には、上述した制限処理および促進処理を実施した場合における冷媒圧力Pmの推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における冷媒圧力Pmの推移の一例を二点鎖線にて示している。図6(d)には、上述した制限処理および促進処理を実施した場合における圧縮機1の運転モードの推移の一例を実線にて示し、上述した制限処理および促進処理を実施しない場合における圧縮機1の運転モードの推移の一例を二点鎖線にて示している。 In FIG. 6A, an example of the transition of the opening degree of the electronic expansion valve 2 when the restriction process and the acceleration process described above are performed is shown by a solid line, and when the restriction process and the acceleration process described above are not performed. An example of transition of the opening degree of the electronic expansion valve 2 is shown by a two-dot chain line. In FIG. 6B, an example of the transition of the set temperature To set by the user through the remote controller 15 is shown by a solid line, and an example of the transition of the detected temperature Tr by the room temperature sensor 14 is shown by a dashed line. In FIG. 6(c), an example of the transition of the refrigerant pressure Pm in the case where the above-mentioned restriction process and the acceleration process are carried out is shown by a solid line, and the transition of the refrigerant pressure Pm in the case where the above-mentioned restriction process and the acceleration process are not carried out. An example is shown by a chain double-dashed line. In FIG. 6D, an example of the transition of the operation mode of the compressor 1 when the above-described restriction process and acceleration process are performed is shown by a solid line, and the compressor when the above-mentioned restriction process and acceleration process are not performed is shown. An example of transition of the operation mode of No. 1 is shown by a two-dot chain line.

同図6に示されるように、圧縮機1がフルロードモードで運転された(タイミングt0〜t1)後、運転モードをフルロードモードからアンロードモードに切り換える(タイミングt1)と、制御装置7は、所定期間T3に渡って、冷媒圧力Pmを監視する(タイミングt1〜t7)。冷媒圧力Pmが閾値P1以上となると、制御装置7は、過熱度SH1に基づいて算出される電子式膨張弁2の開度に対して所定開度θaを減算補正する制限処理を開始する(タイミングt5)。この制限処理は、所定期間T1に渡って継続する(タイミングt5〜t6)。 As shown in FIG. 6, when the compressor 1 is operated in the full load mode (timing t0 to t1) and then the operation mode is switched from the full load mode to the unload mode (timing t1), the control device 7 is activated. , The refrigerant pressure Pm is monitored over a predetermined period T3 (timing t1 to t7). When the refrigerant pressure Pm becomes equal to or higher than the threshold value P1, the control device 7 starts the limiting process of subtracting and correcting the predetermined opening degree θa with respect to the opening degree of the electronic expansion valve 2 calculated based on the superheat degree SH1 (timing. t5). This restriction process continues for a predetermined period T1 (timing t5 to t6).

本実施の形態においては、実施の形態1で説明した効果と同様の効果を奏することに加えて、以下の効果を奏する。 In addition to the same effects as the effects described in the first embodiment, the present embodiment has the following effects.

・冷媒圧力Pmが閾値P1以上となったと判断する場合、制限処理を開始し、冷媒圧力Pmが閾値P1未満と判断する場合は、制限処理を開始しない。このため、冷媒圧力Pが、十分に低いにも関わらず制限処理が開始され、循環する冷媒量が過度に減少することを抑制することができる。従って、冷房能力の低下を抑制することができる。 When the refrigerant pressure Pm is determined to be equal to or higher than the threshold P1, the limiting process is started, and when the refrigerant pressure Pm is determined to be less than the threshold P1, the limiting process is not started. Therefore, it is possible to prevent the restriction process from being started and the amount of the circulating refrigerant to be excessively reduced even though the refrigerant pressure P is sufficiently low. Therefore, it is possible to suppress a decrease in cooling capacity.

(実施の形態3)
実施の形態3の空気調和装置10の制御方法について、先の図1〜3の他、更に図7を併せ参照して説明する。なお、特に断りの無い場合、同一符号は同一の構成を示し、実施の形態1と同様の処理については、同一のステップ番号を付すことによりその詳細な説明を適宜割愛する。
(Embodiment 3)
A control method of the air-conditioning apparatus 10 according to the third embodiment will be described with reference to FIGS. It should be noted that, unless otherwise specified, the same reference numerals indicate the same configurations, and the same processes as those in the first embodiment are denoted by the same step numbers, and the detailed description thereof will be appropriately omitted.

図7は、実施の形態3に係る空気調和装置10の制御フローチャートの説明図である。図7を参照して実施の形態3に係る制御装置7の動作について説明する。図7に示す制御フローチャートは、図3のフローチャートに、空気調和装置10の起動時の処理(ステップS1〜3)を追加したものであり、その他のステップについては同様である。そこで、同様の制御内容については説明を省略する。 FIG. 7 is an explanatory diagram of a control flowchart of the air-conditioning apparatus 10 according to the third embodiment. The operation of the control device 7 according to the third embodiment will be described with reference to FIG. 7. The control flowchart shown in FIG. 7 is obtained by adding processing (steps S1 to S3) at the time of starting the air conditioning apparatus 10 to the flowchart of FIG. 3, and the other steps are the same. Therefore, description of similar control contents is omitted.

空気調和装置10の起動時、圧縮機1内の冷媒は低温状態にあるため、冷媒が圧縮機1の潤滑油に溶け込みやすい状態にある。圧縮機1内で潤滑油に冷媒が多く溶け込んでいると、圧縮機1の起動時に圧縮機1内が減圧されることによって潤滑油内の冷媒が急激に蒸発するいわゆるオイルフォーミングが発生するおそれがある。オイルフォーミングが発生すると、圧縮機1内で泡状となった潤滑油が圧縮機1の外部に排出されてしまう恐れがある。 When the air conditioner 10 is started, the refrigerant in the compressor 1 is in a low temperature state, so that the refrigerant easily dissolves in the lubricating oil of the compressor 1. If a large amount of the refrigerant is dissolved in the lubricating oil in the compressor 1, the pressure inside the compressor 1 is reduced when the compressor 1 is started, which may cause so-called oil forming in which the refrigerant in the lubricating oil is rapidly evaporated. is there. When oil forming occurs, the foamed lubricating oil in the compressor 1 may be discharged to the outside of the compressor 1.

そこで、本実施の形態では、空気調和装置10の起動時に電子式膨張弁2の開度を所定開度θc(特許請求の範囲における起動時開度)に固定することで、起動時における圧縮機1への冷媒流入量を増加させ、圧縮機1内の圧力の低下を抑制する。また、空気調和装置10の起動時における圧縮機1の運転モードをアンロードモードとし、圧縮機1からの冷媒排出量を低下させることで、更に好適に圧縮機1内の圧力の低下を抑制する。 Therefore, in the present embodiment, when the air conditioner 10 is started, the opening degree of the electronic expansion valve 2 is fixed to a predetermined opening degree θc (starting opening degree in claims), so that the compressor at the time of starting is fixed. The amount of refrigerant flowing into the compressor 1 is increased, and the decrease in the pressure inside the compressor 1 is suppressed. In addition, the operation mode of the compressor 1 when the air conditioner 10 is started is set to the unload mode, and the refrigerant discharge amount from the compressor 1 is reduced, so that the reduction in the pressure in the compressor 1 is more preferably suppressed. ..

図7を参照しながら、本実施の形態における空気調和装置10の起動時の処理について説明する。制御装置7は、圧縮機1の運転が開始され、空気調和装置10の運転が開始されると、電子式膨張弁2の開度を予め定められた所定開度θcに固定する(ステップS1)。所定開度θcは、圧縮機1の起動時に圧縮機1から冷媒が吐出されることで圧縮機1内が減圧されても、オイルフォーミングが発生しない量の冷媒を圧縮機1内に供給するのに必要な開度であり、任意に設定される。電子式膨張弁2がとり得る最大の開度であることが最も好ましい。 The process at the time of starting the air conditioning apparatus 10 in the present embodiment will be described with reference to FIG. 7. When the operation of the compressor 1 is started and the operation of the air conditioner 10 is started, the control device 7 fixes the opening degree of the electronic expansion valve 2 to a predetermined opening degree θc (step S1). .. The predetermined opening degree θc supplies the refrigerant in an amount such that oil forming does not occur even if the inside of the compressor 1 is depressurized by discharging the refrigerant from the compressor 1 when the compressor 1 is started. It is the opening required for, and is set arbitrarily. Most preferably, it is the maximum opening that the electronic expansion valve 2 can take.

次に、制御装置7は、圧縮機1の運転モードをアンロードモードとする(ステップS2)。その後、制御装置7は、空気調和装置10の運転が開始されてからの経過期間Tdが所定期間T4以上であるか否かを判断する(ステップS3)。所定期間T4は、空気調和装置10の起動が完了し、定常状態に移行するのに必要な期間である。例えば、空気調和装置10の起動後、過熱度SH1が一定の範囲に収束するのに必要な期間を予め求めて測定し、この期間を所定期間T4とすることができる。または、圧縮機1から排出された冷媒が、冷媒管路20を循環して再び圧縮機1に戻ってくるまでの期間を予め測定し、この期間を所定期間T4とすることができる。 Next, the controller 7 sets the operation mode of the compressor 1 to the unload mode (step S2). After that, the control device 7 determines whether or not the elapsed period Td from the start of the operation of the air conditioner 10 is the predetermined period T4 or more (step S3). The predetermined period T4 is a period required to complete the start-up of the air conditioner 10 and transition to the steady state. For example, after the air conditioner 10 is started, the period required for the superheat degree SH1 to converge to a certain range is obtained in advance and measured, and this period can be set as the predetermined period T4. Alternatively, the period until the refrigerant discharged from the compressor 1 circulates in the refrigerant pipe 20 and returns to the compressor 1 again can be measured in advance, and this period can be set as the predetermined period T4.

空気調和装置10の運転が開始されてからの経過期間Tdが所定期間T4未満であると判断する場合(ステップS3;NO)、ステップS3に戻る。一方、空気調和装置10の運転が開始されてからの経過期間Tdが所定期間T4以上であると判断する場合(ステップS3;YES)、ステップS10に進む。 When it is determined that the elapsed period Td from the start of the operation of the air conditioner 10 is less than the predetermined period T4 (step S3; NO), the process returns to step S3. On the other hand, when it is determined that the elapsed period Td from the start of the operation of the air conditioner 10 is the predetermined period T4 or more (step S3; YES), the process proceeds to step S10.

本実施の形態においては、実施の形態1、2で説明した効果と同様の効果を奏することに加えて、以下の効果を奏する。
・空気調和装置10の起動時に、電子式膨張弁2の開度を所定開度θcに固定するとともに、圧縮機1の運転モードをアンロードモードとするため、空気調和装置10の起動時における圧縮機1内の圧力低下を抑制することができる。従って、空気調和装置10の起動時における液バックおよびオイルフォーミングの発生を抑制することができる。
In addition to the same effects as those described in the first and second embodiments, the present embodiment has the following effects.
When the air conditioner 10 is started, the opening degree of the electronic expansion valve 2 is fixed to the predetermined opening degree θc, and the operation mode of the compressor 1 is set to the unload mode. The pressure drop in the machine 1 can be suppressed. Therefore, it is possible to suppress the occurrence of the liquid bag and the oil forming when the air conditioner 10 is started.

(実施の形態4)
実施の形態4の空気調和装置10を、図8、図9を用いて説明する。この実施の形態4では、実施の形態1または2で説明した空気調和装置10を鉄道車両に適用した例について説明する。なお、特に断りの無い場合、同一符号は同一の構成を示し、実施の形態1または2と同様の処理については、同一のステップ番号を付すことによりその詳細な説明を適宜割愛する。
同図8に、本実施の形態における空気調和装置10が搭載された車両70の外観図を示す。同図8には、空気調和装置10を車両の屋根上に設置した場合を示しているが、空気調和装置10は、車両の床下に設置してもよい。
(Embodiment 4)
The air conditioning apparatus 10 according to the fourth embodiment will be described with reference to FIGS. 8 and 9. In this Embodiment 4, an example in which the air-conditioning apparatus 10 described in Embodiment 1 or 2 is applied to a railway vehicle will be described. It should be noted that, unless otherwise specified, the same reference numerals indicate the same configurations, and the same steps as those in the first or second embodiment are denoted by the same step numbers, and the detailed description thereof will be appropriately omitted.
FIG. 8 shows an external view of a vehicle 70 equipped with the air conditioning apparatus 10 according to the present embodiment. Although FIG. 8 shows the case where the air conditioning apparatus 10 is installed on the roof of the vehicle, the air conditioning apparatus 10 may be installed under the floor of the vehicle.

図9に示すように、本実施の形態では、圧縮機1の軸心が水平面に対して傾斜角度A傾斜するように、吐出側を上側にして傾けて配置されている。傾斜角度Aは、0°〜15°が好ましく、0°〜10°がより好ましく、0°〜5°が最も好ましい。 As shown in FIG. 9, in the present embodiment, the compressor 1 is disposed with the discharge side facing upward so that the axial center is inclined at an inclination angle A with respect to the horizontal plane. The inclination angle A is preferably 0° to 15°, more preferably 0° to 10°, and most preferably 0° to 5°.

鉄道車両に空気調和装置10を搭載するにあたっては、設置するスペースに限りがあり、特に高さ方向に空間の余裕がない事例が多い。このため、空気調和装置10の低背化が要求される。 When installing the air conditioner 10 on a railroad vehicle, there are many cases where the space to install the air conditioner 10 is limited, and there is particularly no space in the height direction. Therefore, it is required to reduce the height of the air conditioner 10.

一方、圧縮機1の内部には、固定渦巻体54や搖動渦巻体55等を潤滑する潤滑油31が貯留されている。低背化を図るため、圧縮機1の軸心が水平面に対して平行に設置された場合、潤滑油31が圧縮冷媒とともに冷媒管路20に流出するおそれがある。また、液バックが発生した場合も同様に、潤滑油31が冷媒管路20に流出するおそれがある。 On the other hand, inside the compressor 1, the lubricating oil 31 that lubricates the fixed spiral body 54, the swing spiral body 55, and the like is stored. When the axial center of the compressor 1 is installed parallel to the horizontal plane in order to achieve a low profile, the lubricating oil 31 may flow out into the refrigerant conduit 20 together with the compressed refrigerant. Further, when liquid back occurs, similarly, the lubricating oil 31 may flow out to the refrigerant pipeline 20.

この点、本実施の形態では、圧縮機1の軸心を水平面に対して傾斜角度A傾斜するように配置しているため、水平面に対して平行に設置された場合よりも、潤滑油の流出を抑制することができる。また、上記各実施の形態1〜3で説明したように、電子式制御弁2の制御を通じて液バックの発生を抑制することができるため、好適に潤滑油の流出を抑制することができる。 In this respect, in the present embodiment, since the axial center of the compressor 1 is arranged so as to be inclined at the inclination angle A with respect to the horizontal plane, the outflow of lubricating oil is greater than that in the case where the compressor 1 is installed parallel to the horizontal plane. Can be suppressed. Further, as described in each of the first to third embodiments, since the occurrence of liquid back can be suppressed through the control of the electronic control valve 2, the outflow of lubricating oil can be suppressed appropriately.

本実施の形態においては、実施の形態1〜3で説明した効果と同様の効果を奏することに加えて、以下の効果を奏する。
・本実施の形態によれば、空気調和装置1の低背化を図ることができるとともに潤滑油31の流出を抑制することができる。
In addition to the same effects as the effects described in the first to third embodiments, the present embodiment has the following effects.
-According to the present embodiment, it is possible to reduce the height of the air conditioner 1 and suppress the outflow of the lubricating oil 31.

(その他の実施の形態)
・図10に示すように、本実施の形態における空気調和装置10は、室内熱交換器4から圧縮機1につながる冷媒管路20の途中に設けられたアキュムレータ28と、冷媒流路を切り換える四方弁29と、圧縮機1から吐出された冷媒を圧縮機1の流入側にバイパスするホットガスバイパス27と、ホットガスバイパス路27の流通/非流通を切り換える電磁弁32とを備えるものとすることができる。
(Other embodiments)
As shown in FIG. 10, the air conditioner 10 according to the present embodiment includes an accumulator 28 provided in the middle of a refrigerant pipe 20 connecting the indoor heat exchanger 4 to the compressor 1, and a four-way refrigerant flow path. A valve 29, a hot gas bypass 27 that bypasses the refrigerant discharged from the compressor 1 to the inflow side of the compressor 1, and an electromagnetic valve 32 that switches between circulation and non-circulation of the hot gas bypass passage 27 are provided. You can

本実施の形態では、暖房運転時、冷媒は、四方弁29の切り換により、圧縮機1で圧縮されて高温高圧のガス状となり、室内熱交換器4で凝縮液化した後、電子式膨張弁2で膨張され、減圧されることで低温低圧の二相状態となり、室外熱交換器3で蒸発ガス化して、アキュムレータ28を通って圧縮機1に戻る。車内空気は、室内熱交換器を通過する際、高温の冷媒と熱交換を行い、高温の空気となり、車内に供給される。冷房時と暖房時においては、上述したように、冷媒回路内の冷媒の流れ方向が異なるだけであり、その構成と動作は同一である。 In the present embodiment, during heating operation, the refrigerant is compressed by the compressor 1 into a high-temperature and high-pressure gaseous state by switching the four-way valve 29, condensed and liquefied in the indoor heat exchanger 4, and then the electronic expansion valve. It is expanded in 2 and reduced in pressure to become a low temperature and low pressure two-phase state, which is vaporized into gas in the outdoor heat exchanger 3 and returned to the compressor 1 through the accumulator 28. When the vehicle interior air passes through the indoor heat exchanger, it exchanges heat with the high temperature refrigerant, becomes high temperature air, and is supplied into the vehicle interior. As described above, only the flow direction of the refrigerant in the refrigerant circuit is different between the cooling time and the heating time, and the configuration and operation are the same.

本実施の形態によれば、潤滑油が圧縮機1から流出した場合であっても、ホットガスバイパス路27を流通して再び圧縮機1に流入するため、圧縮機1における潤滑油の枯渇を抑制することができる。また、液状の冷媒はアキュムレータに貯留されるため、液バックの発生をより効果的に抑制することができる。 According to the present embodiment, even when the lubricating oil flows out of the compressor 1, the lubricating oil flows through the hot gas bypass passage 27 and flows into the compressor 1 again, so that the lubricating oil in the compressor 1 is exhausted. Can be suppressed. Further, since the liquid refrigerant is stored in the accumulator, the occurrence of liquid back can be suppressed more effectively.

なお、上記各実施の形態では、検出温度Trから設定温度Toを減算した値をΔTとしていたが、本実施の形態では、検出温度Trから設定温度Toを減算した値の絶対値を偏差ΔTとすることが好ましい。 In each of the above-described embodiments, the value obtained by subtracting the set temperature To from the detected temperature Tr is set as ΔT, but in the present embodiment, the absolute value of the value obtained by subtracting the set temperature To from the detected temperature Tr is defined as the deviation ΔT. Preferably.

・上記各実施の形態では、高圧制御弁8および低圧制御弁9を、冷媒の流通/非流通を切り換える電磁弁からなるものとしたが、本発明はこれに限られるものではない。例えば、高圧制御弁8および低圧制御弁9を開度調整が可能な電動弁からなるリニア弁としてもよい。 In each of the above embodiments, the high pressure control valve 8 and the low pressure control valve 9 are electromagnetic valves that switch between flowing and non-circulating the refrigerant, but the present invention is not limited to this. For example, the high pressure control valve 8 and the low pressure control valve 9 may be linear valves that are electrically operated valves that can adjust the opening.

・上記実施の形態では、圧縮機1に流入する冷媒の温度と圧力に基づいて過熱度SH1を算出するものとしたが、本発明はこれに限られるものではない。室内熱交換器4の入口部分と出口部分に温度センサを設け、これら温度センサの検出温度に基づいて過熱度SH1を算出してもよい。この場合であっても、上記各実施の形態で説明した効果と同様の効果を奏することができる。 In the above embodiment, the superheat degree SH1 is calculated based on the temperature and pressure of the refrigerant flowing into the compressor 1, but the present invention is not limited to this. It is also possible to provide temperature sensors at the inlet and outlet of the indoor heat exchanger 4 and calculate the superheat degree SH1 based on the temperatures detected by these temperature sensors. Even in this case, the same effect as the effect described in each of the above-described embodiments can be obtained.

・上記実施の形態3では、鉄道車両に搭載される例を説明したが、本発明はこれに限られるものではなく、家屋、ビル、倉庫、自動車などに設置されるものであってもよい。これらの場合であっても、上記実施の形態3で説明した効果と同様の効果を奏することができる。 In the above-described third embodiment, an example in which it is mounted on a railway vehicle has been described, but the present invention is not limited to this, and may be installed in a house, a building, a warehouse, an automobile, or the like. Even in these cases, the same effect as the effect described in the third embodiment can be obtained.

・上記各実施の形態の制限処理では、過熱度SH1に基づいて設定される電子制御弁2の開度に予め定められる所定開度θaを減算補正するようにしたが、本発明の制限処理はこれに限られるものではなく、電子式膨張弁2の開度を過熱度SH1に基づいて設定される開度より小さくするものであればよい。例えば、電子式膨張弁2がとり得る最小開度としてもよいし、制限処理の開始時の冷媒圧力Pmが大きいときほど、所定開度θaを大きくしてもよい。または、制限処理を実行している間、冷媒圧力Pmを監視し、この監視結果に基づいて所定開度θaを調整してもよい。 In the limiting process of each of the above-described embodiments, the predetermined opening degree θa predetermined to the opening degree of the electronic control valve 2 set based on the superheat degree SH1 is subtracted and corrected. The invention is not limited to this, and the opening degree of the electronic expansion valve 2 may be smaller than the opening degree set based on the superheat degree SH1. For example, it may be set to the minimum opening that the electronic expansion valve 2 can take, or the predetermined opening θa may be set to be larger as the refrigerant pressure Pm at the start of the restriction process is larger. Alternatively, the refrigerant pressure Pm may be monitored while the restriction process is being executed, and the predetermined opening degree θa may be adjusted based on the monitoring result.

・上記各実施の形態の制限処理は、予め定められた所定期間T1継続した後、終了するようにしたが、本発明における制限処理の実施期間は、所定期間T1に限られるものではなく、適宜変更することができる。例えば、制限処理の開始時の冷媒圧力Pmが大きいほど、所定期間T1を長い期間に設定してもよい。または、冷媒圧力Pmが所定の冷媒圧力P2まで低下したことをもって制限処理を終了してもよい。冷媒圧力P2は、低圧冷媒管路25を、室内熱交換器4の熱交換能力の上限に相当する量の冷媒が通過する場合における冷媒圧力とすることが好ましい。 Although the restriction process of each of the above-described embodiments is configured to be terminated after continuing for a predetermined period T1 set in advance, the execution period of the restriction process of the present invention is not limited to the predetermined period T1 and may be appropriately changed. Can be changed. For example, the predetermined period T1 may be set to be longer as the refrigerant pressure Pm at the start of the restriction process is higher. Alternatively, the restriction process may be terminated when the refrigerant pressure Pm has dropped to the predetermined refrigerant pressure P2. The refrigerant pressure P2 is preferably the refrigerant pressure when the amount of refrigerant corresponding to the upper limit of the heat exchange capacity of the indoor heat exchanger 4 passes through the low-pressure refrigerant pipe 25.

・上記各実施の形態の促進処理では、過熱度SH1に基づいて設定される電子制御弁2の開度に予め定められる所定開度θbを加算補正するようにしたが、本発明の促進処理はこれに限られるものではなく、電子式膨張弁2の開度を過熱度SH1に基づいて設定される開度より大きくするものであればよい。例えば、電子式膨張弁2がとり得る最大開度としてもよいし、促進処理の開始時の冷媒圧力Pmが小さいときほど所定開度θbを小さくしてもよい。または、促進処理を実行している間、冷媒圧力Pmを監視し、この監視結果に基づいて所定開度θbを調整してもよい。 In the acceleration process of each of the above-described embodiments, the predetermined opening degree θb that is set in advance is added to the opening degree of the electronic control valve 2 that is set based on the superheat degree SH1. The opening degree of the electronic expansion valve 2 is not limited to this, and may be set to be larger than the opening degree set based on the superheat degree SH1. For example, the maximum opening that can be taken by the electronic expansion valve 2 may be set, or the predetermined opening θb may be set smaller as the refrigerant pressure Pm at the start of the acceleration process is smaller. Alternatively, the refrigerant pressure Pm may be monitored while the acceleration process is being executed, and the predetermined opening degree θb may be adjusted based on the monitoring result.

・上記各実施の形態の促進処理は、予め定められた所定期間T2継続した後、終了するようにしたが、本発明における促進処理の実施期間は、所定期間T2に限られるものではなく、適宜変更することができる。例えば、促進処理の開始時の冷媒圧力Pmが小さいときほど、所定期間T2を長い期間に設定してもよい。または、または、冷媒圧力Pmが予め定めた冷媒圧力P3まで上昇したことをもって制限処理を終了してもよい。 The promotion process of each of the above embodiments is configured to be terminated after continuing for a predetermined period T2 set in advance, but the implementation period of the promotion process in the present invention is not limited to the predetermined period T2, and may be appropriately changed. Can be changed. For example, the predetermined period T2 may be set to be longer as the refrigerant pressure Pm at the start of the acceleration process is smaller. Alternatively, or if the refrigerant pressure Pm rises to a predetermined refrigerant pressure P3, the limiting process may be ended.

1 圧縮機、2 電子式膨張弁、3 室外熱交換器、4 室内熱交換器、7 制御装置、8 高圧制御弁、9 低圧制御弁、10 空気調和装置、11 冷媒温度センサ、12 冷媒圧力センサ、14 室温センサ、15 リモコン、20 冷媒管路、21 高圧制御冷媒通路、22 低圧制御冷媒通路、23 制御圧力導入管、25 低圧冷媒管路、26 高圧冷媒管路、27 ホットガスバイパス路、28 アキュムレータ、29 四方弁、32 電磁弁、50 密閉容器、51 固定スクロール、52 搖動スクロール、53 吐出路、54 固定渦巻体、55 搖動渦巻体、60 容量制御機構、61 背圧通路、62 背圧室、63 コイルスプリング、64 バイパス弁、65 バイパス通路。 1 compressor, 2 electronic expansion valve, 3 outdoor heat exchanger, 4 indoor heat exchanger, 7 control device, 8 high pressure control valve, 9 low pressure control valve, 10 air conditioner, 11 refrigerant temperature sensor, 12 refrigerant pressure sensor , 14 room temperature sensor, 15 remote control, 20 refrigerant line, 21 high pressure control refrigerant passage, 22 low pressure control refrigerant passage, 23 control pressure introducing pipe, 25 low pressure refrigerant pipe, 26 high pressure refrigerant pipe, 27 hot gas bypass pipe, 28 Accumulator, 29 four-way valve, 32 solenoid valve, 50 closed container, 51 fixed scroll, 52 rocking scroll, 53 discharge passage, 54 fixed spiral body, 55 swinging spiral body, 60 volume control mechanism, 61 back pressure passage, 62 back pressure chamber , 63 coil springs, 64 bypass valves, 65 bypass passages.

Claims (11)

圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、
前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、
前記バイパス通路を開閉するバイパス弁と、
冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、
前記制御装置は、前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御にて設定される開度に対して所定開度だけ小さい値に補正する制限処理を開始し、
前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果に基づき前記所定開度を設定する
ことを特徴とする空気調和装置。
An air conditioner having a refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve are connected by a refrigerant pipe,
An intermediate compression chamber in which a refrigerant in the middle of compression of the compressor is present, and a bypass passage communicating with a low pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber is present,
A bypass valve for opening and closing the bypass passage,
A control device for performing superheat control for setting the opening degree of the electronic expansion valve based on the superheat of the refrigerant,
The control device opens the opening of the electronic expansion valve to a predetermined opening with respect to the opening set by the superheat control based on the switching of the bypass valve from the closed state to the open state. restriction processing start the corrected to a value smaller by degrees,
The air conditioner , wherein the control unit sets the predetermined opening degree based on a detection result of a pressure detection unit that detects the pressure of the refrigerant flowing into the compressor .
請求項1に記載の空気調和装置であって、The air conditioner according to claim 1, wherein
前記所定開度は、前記制限処理の開始時の前記冷媒の圧力が大きいときほど、大きく設定されるThe predetermined opening degree is set to be larger as the pressure of the refrigerant at the start of the limiting process is higher.
ことを特徴とする空気調和装置。An air conditioner characterized by the above.
請求項1に記載の空気調和装置であって、The air conditioner according to claim 1, wherein
前記制限処理を実行している間、前記冷媒の圧力が監視され、監視結果に基づいて、前記所定開度が調整されるWhile performing the limiting process, the pressure of the refrigerant is monitored, and the predetermined opening is adjusted based on the monitoring result.
ことを特徴とする空気調和装置。An air conditioner characterized by the above.
圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、
前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、
前記バイパス通路を開閉するバイパス弁と、
冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、
前記制御装置は、前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御にて設定される値よりも小さい値に補正する制限処理を開始し、
前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果が第1所定圧力以上であることを前記制限処理の開始条件とする
ことを特徴とする空気調和装置。
An air conditioner having a refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve are connected by a refrigerant pipe,
An intermediate compression chamber in which a refrigerant in the middle of compression of the compressor is present, and a bypass passage communicating with a low pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber is present,
A bypass valve for opening and closing the bypass passage,
A control device for performing superheat control for setting the opening degree of the electronic expansion valve based on the superheat of the refrigerant,
The control device corrects the opening degree of the electronic expansion valve to a value smaller than a value set by the superheat control based on the switching of the bypass valve from the closed state to the open state. the restriction process to begin,
The air conditioner is characterized in that the control device sets the detection condition of the pressure detection means for detecting the pressure of the refrigerant flowing into the compressor to be equal to or higher than a first predetermined pressure as a start condition of the restriction process .
圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路を有する空気調和装置であって、
前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間と連通するバイパス通路と、
前記バイパス通路を開閉するバイパス弁と、
冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御を実施する制御装置とを備え、
前記制御装置は、前記バイパス弁を開弁状態から閉弁状態に切り換える切り換え要求を検出すると、前記電子膨張弁の開度を前記過熱度制御にて設定される開度に対して所定開度だけ大きい値に補正する促進処理を開始し、その後、前記バイパス弁を開弁状態から閉弁状態に切り換え、
前記制御装置は、前記圧縮機に流入する冷媒の圧力を検出する圧力検出手段の検出結果に基づき前記所定開度を設定する
ことを特徴とする空気調和装置。
An air conditioner having a refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve are connected by a refrigerant pipe,
An intermediate compression chamber in which a refrigerant in the middle of compression of the compressor exists, and a bypass passage communicating with a low-pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber exists,
A bypass valve for opening and closing the bypass passage,
A control device for performing superheat control for setting the opening degree of the electronic expansion valve based on the superheat of the refrigerant,
Wherein the controller detects a change request to switch to the closed state the bypass valve from the open state, the predetermined opening degree with respect to the opening set an opening degree of the electronic expansion valve by the superheat control start the promotion processing for correcting to a large value only, then conversion example off the bypass valve from the open state to the closed state,
The air conditioner , wherein the control unit sets the predetermined opening degree based on a detection result of a pressure detection unit that detects the pressure of the refrigerant flowing into the compressor .
請求項5に記載の空気調和装置であって、The air conditioner according to claim 5,
前記所定開度は、前記促進処理の開始時の前記冷媒の圧力が小さいときほど、小さく設定されるThe predetermined opening degree is set smaller as the pressure of the refrigerant at the start of the promotion processing is smaller.
ことを特徴とする空気調和装置。An air conditioner characterized by the above.
請求項5に記載の空気調和装置であって、The air conditioner according to claim 5,
前記促進処理を実行している間、前記冷媒の圧力が監視され、監視結果に基づいて、前記所定開度が調整されるWhile executing the acceleration process, the pressure of the refrigerant is monitored, and the predetermined opening is adjusted based on the monitoring result.
ことを特徴とする空気調和装置。An air conditioner characterized by the above.
請求項1〜のいずれか1項に記載の空気調和装置であって、
前記圧縮機の起動時には、前記電子式膨張弁の開度を起動時開度に設定し、前記バイパス弁を開状態に設定する
ことを特徴とする空気調和装置。
The air conditioner according to any one of claims 1 to 9 ,
Wherein the compressor startup, setting the opening degree of the electronic expansion valve during startup opening, the air conditioning apparatus characterized by setting the bypass valve to the open valve state.
請求項1〜のいずれか1項に記載の空気調和装置を車両に搭載した鉄道車両用空気調和装置であって、
前記圧縮機が水平面に対して傾斜して配置される
ことを特徴とする鉄道車両用空気調和装置。
An air conditioner for a railway vehicle, comprising the air conditioner according to any one of claims 1 to 8 mounted on a vehicle,
The air conditioner for a railway vehicle, wherein the compressor is arranged so as to be inclined with respect to a horizontal plane.
圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路と、
前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間とを連通するバイパス通路と、
前記バイパス通路を開閉するバイパス弁と、
を備えた空気調和装置の制御方法であって、
冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御工程と、
前記バイパス弁が閉弁状態から開弁状態に切り換えられたことに基づいて、前記電子式膨張弁の開度を前記過熱度制御工程にて設定される開度に対して所定開度だけ小さい値に補正する制限工程と、
を備え、
前記所定開度は、前記圧縮機に流入する冷媒の圧力に基づき設定される
ことを特徴とする空気調和装置の制御方法。
A refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve are connected by a refrigerant pipe line,
An intermediate compression chamber in which a refrigerant in the middle of compression of the compressor is present, and a bypass passage communicating with a low pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber is present,
A bypass valve for opening and closing the bypass passage,
A method for controlling an air conditioner comprising:
A superheat control step of setting the opening degree of the electronic expansion valve based on the superheat of the refrigerant,
Based on the bypass valve being switched from the closed state to the open state, the opening degree of the electronic expansion valve is a value smaller than the opening degree set in the superheat degree control step by a predetermined opening degree. And the limiting process to correct
Bei to give a,
The said opening degree is set based on the pressure of the refrigerant which flows into the said compressor , The control method of the air conditioning apparatus characterized by the above-mentioned .
圧縮機、室外熱交換器、室内熱交換器および電子式膨張弁を冷媒管路で接続した冷媒回路と、
前記圧縮機の圧縮途中の冷媒が存在する中間圧縮室と、前記中間圧縮室の冷媒より低圧の冷媒が存在する低圧空間と連通するバイパス通路と、
前記バイパス通路を開閉するバイパス弁と、
を備えた空気調和装置の制御方法であって、
冷媒の過熱度に基づいて前記電子式膨張弁の開度を設定する過熱度制御工程と、
前記バイパス弁を開弁状態から閉弁状態に切り換える切り換え要求を検出すると、前記電子膨張弁の開度を前記過熱度制御工程にて設定される開度に対して所定開度だけ大きい値に補正する促進工程と、
を備え、
前記所定開度は、前記圧縮機に流入する冷媒の圧力に基づき設定される
ことを特徴とする空気調和装置の制御方法。
A refrigerant circuit in which a compressor, an outdoor heat exchanger, an indoor heat exchanger and an electronic expansion valve are connected by a refrigerant pipe line,
An intermediate compression chamber in which a refrigerant in the middle of compression of the compressor exists, and a bypass passage communicating with a low-pressure space in which a refrigerant having a lower pressure than the refrigerant in the intermediate compression chamber exists,
A bypass valve for opening and closing the bypass passage,
A method for controlling an air conditioner comprising:
A superheat control step of setting the opening degree of the electronic expansion valve based on the superheat of the refrigerant,
Upon detecting a change request to switch to the closed state the bypass valve from the open state, to a value larger by a predetermined angle with respect to the opening set an opening degree of the electronic expansion valve in the superheat degree control process A facilitating process to correct,
Bei to give a,
The said opening degree is set based on the pressure of the refrigerant which flows into the said compressor , The control method of the air conditioning apparatus characterized by the above-mentioned .
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