JP6257809B2 - Refrigeration cycle equipment - Google Patents

Refrigeration cycle equipment Download PDF

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JP6257809B2
JP6257809B2 JP2016571610A JP2016571610A JP6257809B2 JP 6257809 B2 JP6257809 B2 JP 6257809B2 JP 2016571610 A JP2016571610 A JP 2016571610A JP 2016571610 A JP2016571610 A JP 2016571610A JP 6257809 B2 JP6257809 B2 JP 6257809B2
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heat exchanger
refrigerant
valve
defrosting operation
side heat
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JPWO2016121068A1 (en
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昂仁 彦根
昂仁 彦根
拓也 伊藤
拓也 伊藤
靖 大越
靖 大越
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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
    • F25B47/00Arrangements for preventing or removing deposits or corrosion, not provided for in another subclass
    • F25B47/02Defrosting cycles
    • F25B47/022Defrosting cycles hot gas defrosting
    • F25B47/025Defrosting cycles hot gas defrosting by reversing the 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
    • 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
    • F25B45/00Arrangements for charging or discharging refrigerant
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/029Control issues
    • F25B2313/0292Control issues related to reversing 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
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/031Sensor arrangements
    • F25B2313/0314Temperature sensors near the indoor heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/04Refrigeration circuit bypassing means
    • F25B2400/0411Refrigeration circuit bypassing means for the expansion valve or capillary tube
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16Receivers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • 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
    • F25B2600/25Control of valves
    • F25B2600/2519On-off valves

Description

本発明は、冷凍サイクル装置に関するものである。   The present invention relates to a refrigeration cycle apparatus.

従来、水を冷却および加熱して冷水および温水を生成する空冷式ヒートポンプチラーなどの冷凍サイクル装置が知られている。従来の冷凍サイクル装置において、低外気温下での温水生成時に、蒸発器として機能する熱源側の空気熱交換器に霜が発生することがある。空気熱交換器に霜が発生すると、外気と冷媒との熱交換が阻害され、冷凍サイクル装置の加熱能力が低下してしまう。そこで、空気熱交換器の霜を融解させるための除霜運転を行うことが知られている。   Conventionally, a refrigeration cycle apparatus such as an air-cooled heat pump chiller that cools and heats water to generate cold water and hot water is known. In a conventional refrigeration cycle apparatus, frost may be generated in an air heat exchanger on the heat source side that functions as an evaporator when hot water is generated under a low outside air temperature. When frost is generated in the air heat exchanger, heat exchange between the outside air and the refrigerant is hindered, and the heating capacity of the refrigeration cycle apparatus is reduced. Therefore, it is known to perform a defrosting operation for melting the frost of the air heat exchanger.

特許文献1には、除霜運転を行う冷凍サイクル装置が提案されている。特許文献1の冷凍サイクル装置では、除霜運転条件が成立した場合に、冷媒流路を反転させ、空気熱交換器を凝縮器として機能させることで、空気熱交換器の霜を融解させる。また、特許文献1の冷凍サイクル装置では、空気熱交換器と水熱交換器との間に設けられた絞り機構(膨張弁)に対して、電磁弁を有するバイパス回路が並列に接続されている。そして、除霜運転開始時に電磁弁を開け、冷媒を水熱交換器側に流すことで、冷媒の供給不足による低圧圧力の低下を抑制する構成となっている。   Patent Document 1 proposes a refrigeration cycle apparatus that performs a defrosting operation. In the refrigeration cycle apparatus of Patent Literature 1, when the defrosting operation condition is satisfied, the refrigerant flow path is reversed, and the air heat exchanger is caused to function as a condenser, thereby melting the frost of the air heat exchanger. Further, in the refrigeration cycle apparatus of Patent Document 1, a bypass circuit having an electromagnetic valve is connected in parallel to a throttle mechanism (expansion valve) provided between the air heat exchanger and the water heat exchanger. . And it is the structure which suppresses the fall of the low pressure pressure by the supply shortage of a refrigerant | coolant by opening a solenoid valve at the time of defrosting operation start, and flowing a refrigerant | coolant to the hydrothermal exchanger side.

特開2012−7800号公報JP 2012-7800 A

ここで、余剰冷媒を溜めるための高圧レシーバを備える従来の冷凍サイクル装置において、冷媒流路を反転させて除霜運転を行う場合、除霜運転の開始時には、高圧レシーバに溜まっている液冷媒が水熱交換器を通って圧縮機に流れ、液バックが発生することがある。このような圧縮機への液バックを抑制するために、圧縮機の吸入側にアキュムレータを設置し、アキュムレータに液冷媒を溜めることが考えられる。しかしながら、アキュムレータは容量が大きく、機械室内において大きな設置スペースが必要となるため、装置の大型化およびコストアップを招いてしまう。   Here, in a conventional refrigeration cycle apparatus including a high-pressure receiver for accumulating excess refrigerant, when performing a defrosting operation by inverting the refrigerant flow path, at the start of the defrosting operation, the liquid refrigerant accumulated in the high-pressure receiver Liquid back may occur through the water heat exchanger and into the compressor. In order to suppress such liquid back to the compressor, it is conceivable to install an accumulator on the suction side of the compressor and store the liquid refrigerant in the accumulator. However, the accumulator has a large capacity and requires a large installation space in the machine room, resulting in an increase in size and cost of the apparatus.

本発明は、上記のような課題を解決するためになされたものであり、除霜運転時などの圧縮機への液バックを抑制する冷凍サイクル装置を提供することを目的とする。   The present invention has been made to solve the above-described problems, and an object of the present invention is to provide a refrigeration cycle apparatus that suppresses liquid back to the compressor during a defrosting operation.

本発明に係る冷凍サイクル装置は、圧縮機、流路切替装置、熱源側熱交換器、第1絞り装置および利用側熱交換器を含む冷媒回路と、第2絞り装置、開閉弁および第2絞り装置と開閉弁との間に接続される高圧レシーバを含み、第1絞り装置に並列に接続される液バック抑制回路と、第2絞り装置および開閉弁を制御する制御部と、を備え、制御部は、除霜運転開始条件が成立した場合、第2絞り装置および開閉弁を閉じ、その後、流路切替装置を切り替えて除霜運転を開始するものであるA refrigeration cycle apparatus according to the present invention includes a refrigerant circuit including a compressor, a flow path switching device, a heat source side heat exchanger, a first expansion device, and a use side heat exchanger, a second expansion device, an on-off valve, and a second restriction. It includes a high pressure receiver is connected between the device and the on-off valve, comprising a liquid back suppression circuit connected in parallel with the first throttle device, and a control unit for controlling the second throttle device and the on-off valve, a control The section closes the second expansion device and the on-off valve when the defrosting operation start condition is satisfied, and then switches the flow path switching device to start the defrosting operation .

本発明に係る冷凍サイクル装置によると、除霜運転開始時または終了時などに圧縮機への液バックを抑制することができる。   According to the refrigeration cycle apparatus according to the present invention, liquid back to the compressor can be suppressed at the start or end of the defrosting operation.

本発明の実施の形態1における冷凍サイクル装置の冷媒回路構成を示す図である。It is a figure which shows the refrigerant circuit structure of the refrigerating-cycle apparatus in Embodiment 1 of this invention. 本発明の実施の形態1における冷凍サイクル装置の制御構成を示す図である。It is a figure which shows the control structure of the refrigerating-cycle apparatus in Embodiment 1 of this invention. 本発明の実施の形態1における除霜運転の流れを示すフローチャートである。It is a flowchart which shows the flow of the defrost operation in Embodiment 1 of this invention. 本発明の実施の形態2における除霜運転終了時の流れを示すフローチャートである。It is a flowchart which shows the flow at the time of completion | finish of the defrost operation in Embodiment 2 of this invention. 従来例における冷凍サイクル装置の冷媒回路構成を示す図である。It is a figure which shows the refrigerant circuit structure of the refrigerating-cycle apparatus in a prior art example.

以下に、本発明における冷凍サイクル装置の実施の形態を図面に基づいて詳細に説明する。
実施の形態1.
図1は、本発明の実施の形態1における冷凍サイクル装置100の冷媒回路構成を示す図である。本実施の形態の冷凍サイクル装置100は、水を冷却および加熱して冷水および温水を生成する空冷式ヒートポンプチラーとして利用される。図1に示すように、冷凍サイクル装置100は、圧縮機11、流路切替装置12、熱源側熱交換器13、ファン14、第1絞り装置15および利用側熱交換器17を含む冷媒回路を備える。また、冷凍サイクル装置100は、第1絞り装置15と並列に接続される、第2絞り装置18、高圧レシーバ16および開閉弁19を含む液バック抑制回路40を備える。さらに、冷凍サイクル装置100は、冷媒回路および液バック抑制回路40を制御する制御部20(図2)を備える。
Embodiments of a refrigeration cycle apparatus according to the present invention will be described below in detail with reference to the drawings.
Embodiment 1 FIG.
FIG. 1 is a diagram showing a refrigerant circuit configuration of a refrigeration cycle apparatus 100 according to Embodiment 1 of the present invention. The refrigeration cycle apparatus 100 of the present embodiment is used as an air-cooled heat pump chiller that cools and heats water to generate cold water and hot water. As shown in FIG. 1, the refrigeration cycle apparatus 100 includes a refrigerant circuit including a compressor 11, a flow switching device 12, a heat source side heat exchanger 13, a fan 14, a first expansion device 15, and a use side heat exchanger 17. Prepare. The refrigeration cycle apparatus 100 further includes a liquid back suppression circuit 40 including a second expansion device 18, a high-pressure receiver 16, and an on-off valve 19 that are connected in parallel with the first expansion device 15. Furthermore, the refrigeration cycle apparatus 100 includes a control unit 20 (FIG. 2) that controls the refrigerant circuit and the liquid back suppression circuit 40.

圧縮機11は、例えば、インバータにより制御されるモータ(図示せず)によって駆動される容積式圧縮機である。流路切替装置12は、冷媒の流れる方向を切り替えるものであり、例えば四方弁で構成される。流路切替装置12は、冷却運転時には、図1の実線で示すように冷媒の流路を切り替え、加熱運転時には、図1に破線で示すように冷媒の流路を切り替える。   The compressor 11 is a positive displacement compressor driven by a motor (not shown) controlled by an inverter, for example. The flow path switching device 12 switches the flow direction of the refrigerant, and is composed of, for example, a four-way valve. The flow path switching device 12 switches the flow path of the refrigerant as shown by the solid line in FIG. 1 during the cooling operation, and switches the flow path of the refrigerant as shown by the broken line in FIG. 1 during the heating operation.

熱源側熱交換器13は、室外の空気と熱交換する空気熱交換器であり、例えば、伝熱管と多数のフィンとからなるクロスフィン式のフィン・アンド・チューブ型の熱交換器で構成される。熱源側熱交換器13は、冷却運転時には冷媒の凝縮器として機能し、加熱運転時には冷媒の蒸発器として機能する。ファン14は、熱源側熱交換器13に空気を供給する送風機であり、例えばファンモータ(図示せず)によって駆動されるプロペラファンからなる。ファン14は、室外空気を吸入し、熱源側熱交換器13によって冷媒との間で熱交換された空気を室外に排出する機能を有する。   The heat source side heat exchanger 13 is an air heat exchanger that exchanges heat with outdoor air. For example, the heat source side heat exchanger 13 includes a cross-fin type fin-and-tube heat exchanger including a heat transfer tube and a large number of fins. The The heat source side heat exchanger 13 functions as a refrigerant condenser during the cooling operation, and functions as a refrigerant evaporator during the heating operation. The fan 14 is a blower that supplies air to the heat source side heat exchanger 13, and includes, for example, a propeller fan driven by a fan motor (not shown). The fan 14 has a function of sucking outdoor air and discharging the air heat-exchanged with the refrigerant by the heat source side heat exchanger 13 to the outside.

第1絞り装置15は、冷媒を減圧して膨張させる機能を有し、例えば電子膨張弁で構成される。第1絞り装置15は、熱源側熱交換器13と利用側熱交換器17との間に直列に接続される。利用側熱交換器17は、利用側の水と熱交換する水熱交換器であり、例えば、プレート式の熱交換器で構成される。利用側熱交換器17は、冷却運転時には冷媒の蒸発器として機能し、加熱運転時には冷媒の凝縮器として機能する。   The first expansion device 15 has a function of decompressing and expanding the refrigerant, and is configured by, for example, an electronic expansion valve. The first expansion device 15 is connected in series between the heat source side heat exchanger 13 and the use side heat exchanger 17. The use-side heat exchanger 17 is a water heat exchanger that exchanges heat with the use-side water, and includes, for example, a plate-type heat exchanger. The use side heat exchanger 17 functions as a refrigerant evaporator during the cooling operation, and functions as a refrigerant condenser during the heating operation.

高圧レシーバ16は、余剰冷媒を溜める機能を有し、第2絞り装置18と開閉弁19との間に直列に接続される。第2絞り装置18は、冷媒を減圧して膨張させる機能を有し、例えば電子膨張弁で構成される。第2絞り装置18は、熱源側熱交換器13と高圧レシーバ16との間に直列に接続される。開閉弁19は、例えば電磁弁で構成され、高圧レシーバ16と利用側熱交換器17との間に直列に接続される。第2絞り装置18、高圧レシーバ16および開閉弁19は、直列に接続されて液バック抑制回路40を構成し、第1絞り装置15に並列に接続される。   The high-pressure receiver 16 has a function of accumulating excess refrigerant, and is connected in series between the second expansion device 18 and the on-off valve 19. The second expansion device 18 has a function of decompressing and expanding the refrigerant, and is configured by, for example, an electronic expansion valve. The second expansion device 18 is connected in series between the heat source side heat exchanger 13 and the high-pressure receiver 16. The on-off valve 19 is composed of, for example, an electromagnetic valve, and is connected in series between the high-pressure receiver 16 and the use side heat exchanger 17. The second expansion device 18, the high-pressure receiver 16 and the on-off valve 19 are connected in series to form a liquid back suppression circuit 40, and are connected in parallel to the first expansion device 15.

なお、冷凍サイクル装置100に使用できる冷媒には、単一冷媒、擬似共沸混合冷媒、非共沸混合冷媒等がある。擬似共沸混合冷媒には、HFC冷媒であるR410A、R404A等がある。この擬似共沸混合冷媒は、非共沸混合冷媒と同様の特性の他、R22の約1.6倍の動作圧力という特性を有している。非共沸混合冷媒には、HFC(ハイドロフルオロカーボン)冷媒であるR407C等がある。この非共沸混合冷媒は、沸点が異なる冷媒の混合物であるので、液相冷媒と気相冷媒との組成比率が異なるという特性を有している。   The refrigerant that can be used in the refrigeration cycle apparatus 100 includes a single refrigerant, a pseudo-azeotropic mixed refrigerant, a non-azeotropic mixed refrigerant, and the like. Examples of the pseudo azeotropic refrigerant mixture include R410A and R404A which are HFC refrigerants. This pseudo azeotrope refrigerant has the same characteristic as that of the non-azeotrope refrigerant and has an operating pressure of about 1.6 times that of R22. Non-azeotropic refrigerant mixture includes R407C, which is an HFC (hydrofluorocarbon) refrigerant. Since this non-azeotropic refrigerant mixture is a mixture of refrigerants having different boiling points, it has a characteristic that the composition ratio of the liquid-phase refrigerant and the gas-phase refrigerant is different.

また、冷凍サイクル装置100には、各種センサが設けられている。詳しくは、熱源側熱交換器13には、熱源側熱交換器13の温度を検出する熱交温度センサ31が設けられている。熱交温度センサ31は、熱源側熱交換器13に付着した霜の温度を検出するものであり、例えば熱源側熱交換器13内の伝熱管に設けられる。また、利用側熱交換器17の出入口には、冷媒の温度を検出する入口温度センサ32および出口温度センサ33がそれぞれ設けられている。入口温度センサ32および出口温度センサ33によって検出された冷媒温度に基づいて、制御部20による第1絞り装置15および第2絞り装置18が制御される。さらに、冷凍サイクル装置100の室外に配置される部分には、外気温度を検出するための外気温度センサ34が設けられている。なお、図1には図示していないが、冷凍サイクル装置100は、冷媒の吸入圧力を検出するセンサ、冷媒の吐出温度を検出するセンサ、熱源側熱交換器13の出入口における冷媒の温度を検出するセンサ等を備えていてもよい。   The refrigeration cycle apparatus 100 is provided with various sensors. Specifically, the heat source side heat exchanger 13 is provided with a heat exchange temperature sensor 31 that detects the temperature of the heat source side heat exchanger 13. The heat exchanger temperature sensor 31 detects the temperature of frost attached to the heat source side heat exchanger 13, and is provided, for example, in a heat transfer tube in the heat source side heat exchanger 13. In addition, an inlet temperature sensor 32 and an outlet temperature sensor 33 that detect the temperature of the refrigerant are respectively provided at the inlet and outlet of the use side heat exchanger 17. Based on the refrigerant temperature detected by the inlet temperature sensor 32 and the outlet temperature sensor 33, the first expansion device 15 and the second expansion device 18 are controlled by the control unit 20. Further, an outside air temperature sensor 34 for detecting the outside air temperature is provided in a portion arranged outside the refrigeration cycle apparatus 100. Although not shown in FIG. 1, the refrigeration cycle apparatus 100 detects a refrigerant suction pressure, a refrigerant discharge temperature sensor, and a refrigerant temperature at the inlet / outlet of the heat source side heat exchanger 13. A sensor or the like may be provided.

図2は、冷凍サイクル装置100の制御構成を示す図である。制御部20は、冷凍サイクル装置100の各部を制御するものであり、マイクロコンピュータまたはDSP(Digital Signal Processor)などで構成される。制御部20は、熱交温度センサ31、入口温度センサ32、出口温度センサ33および外気温度センサ34を含む各種センサの検出結果に基づいて、圧縮機11の回転周波数、流路切替装置12の切り替え、ファン14の送風量、第1絞り装置15および第2絞り装置18の開度、ならびに開閉弁19の開閉などを制御する。   FIG. 2 is a diagram illustrating a control configuration of the refrigeration cycle apparatus 100. The control unit 20 controls each unit of the refrigeration cycle apparatus 100, and includes a microcomputer or a DSP (Digital Signal Processor). The control unit 20 switches the rotation frequency of the compressor 11 and the flow path switching device 12 based on the detection results of various sensors including the heat exchange temperature sensor 31, the inlet temperature sensor 32, the outlet temperature sensor 33, and the outside air temperature sensor 34. The air flow rate of the fan 14, the opening degree of the first throttling device 15 and the second throttling device 18, and the opening and closing of the on-off valve 19 are controlled.

次に、冷凍サイクル装置100の動作について説明する。まず、冷凍サイクル装置100における冷却運転時の動作について説明する。冷却運転時には、流路切替装置12によって図1の実線で示すように冷媒の流路が切り替えられる。また、開閉弁19は開けられた状態で固定され、第1絞り装置15および第2絞り装置18は制御部20によって過熱度に基づいて開度が制御される。具体的には、制御部20は、入口温度センサ32および出口温度センサ33で検出される温度から求められる過熱度(圧縮機11の吸入過熱度)が目標値(例えば3℃〜5℃)になるように、第1絞り装置15および第2絞り装置18の開度を決定する。   Next, the operation of the refrigeration cycle apparatus 100 will be described. First, the operation | movement at the time of the cooling operation in the refrigerating-cycle apparatus 100 is demonstrated. During the cooling operation, the flow path of the refrigerant is switched by the flow path switching device 12 as shown by the solid line in FIG. The opening / closing valve 19 is fixed in an opened state, and the opening degree of the first expansion device 15 and the second expansion device 18 is controlled by the control unit 20 based on the degree of superheat. Specifically, the control unit 20 sets the superheat degree (suction superheat degree of the compressor 11) obtained from the temperatures detected by the inlet temperature sensor 32 and the outlet temperature sensor 33 to a target value (for example, 3 ° C to 5 ° C). Thus, the opening degree of the first expansion device 15 and the second expansion device 18 is determined.

圧縮機11によって圧縮および吐出された高温高圧のガス冷媒は、流路切替装置12を通って熱源側熱交換器13へ流入する。熱源側熱交換器13へ流入した高温高圧の冷媒は、室外空気等に対して放熱し、凝縮されて高圧の液冷媒となる。熱源側熱交換器13を流出した高圧の液冷媒は、第1絞り装置15へ流入し、膨張および減圧されて、低温低圧の気液二相冷媒となる。第1絞り装置15から流出した気液二相冷媒は、利用側熱交換器17へ流入する。また、このとき、余剰冷媒が第2絞り装置18を通って高圧レシーバ16に溜められる。利用側熱交換器17へ流入した気液二相冷媒は、水と熱交換して蒸発し、低温低圧のガス冷媒となる。利用側熱交換器17から流出したガス冷媒は、圧縮機11へ吸入され、再び圧縮される。   The high-temperature and high-pressure gas refrigerant compressed and discharged by the compressor 11 flows into the heat source side heat exchanger 13 through the flow path switching device 12. The high-temperature and high-pressure refrigerant that has flowed into the heat source side heat exchanger 13 dissipates heat to the outdoor air or the like, and is condensed to become a high-pressure liquid refrigerant. The high-pressure liquid refrigerant that has flowed out of the heat source side heat exchanger 13 flows into the first expansion device 15 and is expanded and depressurized to become a low-temperature and low-pressure gas-liquid two-phase refrigerant. The gas-liquid two-phase refrigerant flowing out from the first expansion device 15 flows into the use side heat exchanger 17. At this time, surplus refrigerant passes through the second expansion device 18 and is stored in the high-pressure receiver 16. The gas-liquid two-phase refrigerant that has flowed into the use-side heat exchanger 17 evaporates by exchanging heat with water and becomes a low-temperature and low-pressure gas refrigerant. The gas refrigerant flowing out from the use side heat exchanger 17 is sucked into the compressor 11 and compressed again.

次に、加熱運転時の動作について説明する。加熱運転時には、流路切替装置12によって図1の破線で示すように冷媒の流路が切り換えられる。また、開閉弁19は開けられた状態で固定され、第1絞り装置15および第2絞り装置18は制御部20によって過冷却度に基づいて開度が制御される。具体的には、制御部20は、入口温度センサ32および出口温度センサ33で検出される温度から求められる利用側熱交換器17出口の過冷却度が目標値(例えば3℃〜5℃)になるように、第1絞り装置15および第2絞り装置18の開度を決定する。   Next, the operation during the heating operation will be described. During the heating operation, the flow path of the refrigerant is switched by the flow path switching device 12 as indicated by the broken line in FIG. The opening / closing valve 19 is fixed in an opened state, and the opening degree of the first expansion device 15 and the second expansion device 18 is controlled by the control unit 20 based on the degree of supercooling. Specifically, the control unit 20 sets the degree of supercooling at the outlet of the use side heat exchanger 17 obtained from the temperatures detected by the inlet temperature sensor 32 and the outlet temperature sensor 33 to a target value (for example, 3 ° C. to 5 ° C.). Thus, the opening degree of the first expansion device 15 and the second expansion device 18 is determined.

圧縮機11によって圧縮、吐出された高温高圧のガス冷媒は、流路切替装置12を通って利用側熱交換器17へ流入する。利用側熱交換器17へ流入した高温高圧の冷媒は、水に対して放熱し、凝縮されて高圧の液冷媒となる。利用側熱交換器17を流出した高圧の液冷媒は、第1絞り装置15へ流入し、膨張および減圧されて、低温低圧の気液二相冷媒となる。第1絞り装置15から流出した気液二相冷媒は、熱源側熱交換器13へ流入する。また、このとき、余剰冷媒が高圧レシーバ16に溜められる。熱源側熱交換器13へ流入した気液二相冷媒は、室外空気と熱交換して蒸発し、低温低圧のガス冷媒となる。熱源側熱交換器13から流出したガス冷媒は、圧縮機11へ吸入され、再び圧縮される。   The high-temperature and high-pressure gas refrigerant compressed and discharged by the compressor 11 flows into the use side heat exchanger 17 through the flow path switching device 12. The high-temperature and high-pressure refrigerant that has flowed into the use-side heat exchanger 17 dissipates heat to water and is condensed to become a high-pressure liquid refrigerant. The high-pressure liquid refrigerant that has flowed out of the use-side heat exchanger 17 flows into the first expansion device 15, is expanded and depressurized, and becomes a low-temperature and low-pressure gas-liquid two-phase refrigerant. The gas-liquid two-phase refrigerant that has flowed out of the first expansion device 15 flows into the heat source side heat exchanger 13. At this time, surplus refrigerant is stored in the high-pressure receiver 16. The gas-liquid two-phase refrigerant that has flowed into the heat source side heat exchanger 13 evaporates by exchanging heat with outdoor air and becomes a low-temperature and low-pressure gas refrigerant. The gas refrigerant flowing out of the heat source side heat exchanger 13 is sucked into the compressor 11 and compressed again.

また、冷凍サイクル装置100は、上記加熱運転時に、熱源側熱交換器13に霜が発生した場合に、熱源側熱交換器13の霜を融解させるための除霜運転を行う。詳しくは、制御部20は、加熱運転時に熱源側熱交換器13の除霜運転開始条件が成立したと判断すると、流路切替装置12を切り替え、熱源側熱交換器13を凝縮器として機能させる冷却運転を行う。また、このとき、制御部20は、第2絞り装置18および開閉弁19を制御して、高圧レシーバ16に溜まっている液冷媒が利用側熱交換器17を通って圧縮機11に流れ、液バックが発生することを抑制する。   The refrigeration cycle apparatus 100 performs a defrosting operation for melting the frost of the heat source side heat exchanger 13 when frost is generated in the heat source side heat exchanger 13 during the heating operation. Specifically, when determining that the defrosting operation start condition of the heat source side heat exchanger 13 is satisfied during the heating operation, the control unit 20 switches the flow path switching device 12 to cause the heat source side heat exchanger 13 to function as a condenser. Perform cooling operation. At this time, the control unit 20 controls the second expansion device 18 and the on-off valve 19 so that the liquid refrigerant accumulated in the high-pressure receiver 16 flows to the compressor 11 through the use side heat exchanger 17, Suppresses the occurrence of back.

図3は、本実施の形態における除霜運転の流れを示すフローチャートである。図3に示すように、まず、制御部20によって加熱運転時に除霜運転開始条件が成立したか否かが判断される(S1)。ここでは、熱源側熱交換器13に設けられた熱交温度センサ31によって検出された熱交温度、または外気温度センサ34によって検出された外気温度が所定の温度(例えば0℃)よりも低い場合に、熱源側熱交換器13に霜が発生し、除霜運転開始条件が成立したと判断される。そして、除霜運転開始条件が成立した場合(S1:YES)、第2絞り装置18が全閉とされ(S2)、開閉弁19も閉じられる(S3)。これにより、高圧レシーバ16内の圧力が高圧の状態で保持され、液冷媒が高圧レシーバ16内に溜められる。そして、この状態で、流路切替装置12が切り替えられ、除霜運転が開始される(S4)。   FIG. 3 is a flowchart showing the flow of the defrosting operation in the present embodiment. As shown in FIG. 3, first, the controller 20 determines whether or not a defrosting operation start condition is satisfied during the heating operation (S1). Here, when the heat exchange temperature detected by the heat exchange temperature sensor 31 provided in the heat source side heat exchanger 13 or the outside air temperature detected by the outside air temperature sensor 34 is lower than a predetermined temperature (for example, 0 ° C.). Further, it is determined that frost is generated in the heat source side heat exchanger 13 and the defrosting operation start condition is satisfied. When the defrosting operation start condition is satisfied (S1: YES), the second expansion device 18 is fully closed (S2), and the on-off valve 19 is also closed (S3). Thereby, the pressure in the high-pressure receiver 16 is maintained at a high pressure, and the liquid refrigerant is stored in the high-pressure receiver 16. In this state, the flow path switching device 12 is switched and the defrosting operation is started (S4).

除霜運転が開始されると、流路切替装置12によって図1の実線で示すように冷媒の流路が切り替えられ、冷却運転時と同様に熱源側熱交換器13が凝縮器として機能する。そして、吸入過熱度に基づいて、第1絞り装置15の開度が制御される(S5)。次に、圧縮機11の吸入過熱度が閾値Bよりも大きいか否かが判断される(S6)。ここで、圧縮機11の吸入過熱度は、出口温度センサ33で検出される利用側熱交換器17の出口冷媒温度と、入口温度センサ32で検出される利用側熱交換器17入口冷媒温度との差として求められる。また、閾値Bは、圧縮機11の吸入過熱度が十分についたことを判断するための値であり、例えば5℃に設定される。   When the defrosting operation is started, the flow path switching device 12 switches the flow path of the refrigerant as shown by the solid line in FIG. 1, and the heat source side heat exchanger 13 functions as a condenser as in the cooling operation. Then, the opening degree of the first expansion device 15 is controlled based on the suction superheat degree (S5). Next, it is determined whether or not the suction superheat degree of the compressor 11 is larger than the threshold value B (S6). Here, the suction superheat degree of the compressor 11 is determined by the outlet refrigerant temperature of the usage side heat exchanger 17 detected by the outlet temperature sensor 33 and the inlet side refrigerant temperature of the usage side heat exchanger 17 detected by the inlet temperature sensor 32. It is calculated as the difference. Further, the threshold value B is a value for determining that the suction superheat degree of the compressor 11 is sufficient, and is set to 5 ° C., for example.

そして、圧縮機11の吸入過熱度が閾値Bよりも大きい場合(S6:YES)、第2絞り装置18が開けられ(S7)、開閉弁19も開けられる(S8)。その後、吸入過熱度に基づいて、第1絞り装置15および第2絞り装置18の開度が制御され(S9)、除霜運転が継続される。そして、除霜運転終了条件が成立したか否かが判断され(S10)、除霜運転終了条件が成立していない場合は(S10:NO)、除霜運転が継続される。ここでは、制御部20によって、熱源側熱交換器13に設けられている熱交温度センサ31によって検出された温度または外気温度センサ34によって検出された温度が所定の温度(例えば10℃)よりも高い場合に、熱源側熱交換器13の霜が融解したとして除霜運転終了条件が成立したと判断する。一方、除霜運転終了条件が成立した場合は(S10:YES)、流路切替装置12が切り替えられる(S11)。これにより、除霜運転が終了し、加熱運転が再開される。   When the suction superheat degree of the compressor 11 is larger than the threshold value B (S6: YES), the second expansion device 18 is opened (S7), and the on-off valve 19 is also opened (S8). Thereafter, the opening degrees of the first expansion device 15 and the second expansion device 18 are controlled based on the suction superheat degree (S9), and the defrosting operation is continued. Then, it is determined whether the defrosting operation end condition is satisfied (S10). If the defrosting operation end condition is not satisfied (S10: NO), the defrosting operation is continued. Here, the temperature detected by the heat exchanger temperature sensor 31 provided in the heat source side heat exchanger 13 or the temperature detected by the outside air temperature sensor 34 by the control unit 20 is higher than a predetermined temperature (for example, 10 ° C.). When it is high, it is determined that the defrosting operation end condition is satisfied, assuming that the frost of the heat source side heat exchanger 13 has melted. On the other hand, when the defrosting operation termination condition is satisfied (S10: YES), the flow path switching device 12 is switched (S11). Thereby, a defrost operation is complete | finished and a heating operation is restarted.

以上のように、本実施の形態では、除霜運転開始条件成立後(S1:YES)であって、除霜運転開始(S4)前に、第2絞り装置18および開閉弁19を閉じることで、高圧レシーバ16に溜まっている液冷媒の圧縮機11への液バックを抑制することができる。また、圧縮機11の吸入過熱度が閾値以上となった場合(すなわち液バックが発生しない状態になった場合)には、第2絞り装置18および開閉弁19を開けて通常制御を行うことで、除霜運転を行うことができる。   As described above, in the present embodiment, after the defrosting operation start condition is satisfied (S1: YES), and before the defrosting operation start (S4), the second expansion device 18 and the on-off valve 19 are closed. And the liquid back to the compressor 11 of the liquid refrigerant collected in the high-pressure receiver 16 can be suppressed. When the suction superheat degree of the compressor 11 is equal to or greater than the threshold value (that is, when the liquid back does not occur), the second throttle device 18 and the on-off valve 19 are opened to perform normal control. The defrosting operation can be performed.

図5は、従来例における冷凍サイクル装置200の冷媒回路構成を示す図である。図5に示すように、従来の冷凍サイクル装置200は、圧縮機1、四方弁2、空気熱交換器3、ファン4、膨張弁5、高圧レシーバ6および水熱交換器7から構成される。膨張弁5は、空気熱交換器3と水熱交換器7との間に直列に接続されており、冷媒回路を流れる冷媒の減圧および流量制御を行う。また、高圧レシーバ6は膨張弁5と水熱交換器7との間に設置され、余剰冷媒を溜める。図5に示す従来例の冷凍サイクル装置200の場合、冷媒流路を反転させて除霜運転を行うと、除霜運転の開始時には、高圧レシーバ6に溜まっている液冷媒が水熱交換器7を通って圧縮機1に流れ、液バックが発生する。これに対し、本実施の形態では、上記のように液バック抑制回路40を備え、制御部20によって第2絞り装置18および開閉弁19を制御することで、液バックを抑制することができる。   FIG. 5 is a diagram showing a refrigerant circuit configuration of the refrigeration cycle apparatus 200 in the conventional example. As shown in FIG. 5, the conventional refrigeration cycle apparatus 200 includes a compressor 1, a four-way valve 2, an air heat exchanger 3, a fan 4, an expansion valve 5, a high-pressure receiver 6, and a water heat exchanger 7. The expansion valve 5 is connected in series between the air heat exchanger 3 and the water heat exchanger 7, and performs pressure reduction and flow rate control of the refrigerant flowing through the refrigerant circuit. Moreover, the high pressure receiver 6 is installed between the expansion valve 5 and the water heat exchanger 7, and accumulates excess refrigerant. In the case of the conventional refrigeration cycle apparatus 200 shown in FIG. 5, when the defrosting operation is performed by reversing the refrigerant flow path, the liquid refrigerant accumulated in the high-pressure receiver 6 is transferred to the water heat exchanger 7 at the start of the defrosting operation. And flows to the compressor 1 to generate a liquid back. In contrast, in the present embodiment, the liquid back suppression circuit 40 is provided as described above, and the liquid back can be suppressed by controlling the second expansion device 18 and the on-off valve 19 by the control unit 20.

実施の形態2.
続いて、本発明の実施の形態2について説明する。上記実施の形態1では、除霜運転開始時における液バックの発生を抑制するために、第2絞り装置18および開閉弁19を制御する構成となっている。ここで、除霜運転開始時だけでなく、除霜運転終了時にも、熱源側熱交換器13に溜まった液冷媒が、圧縮機1へ戻って液バックが発生することがある。そこで、実施の形態2では、除霜運転終了時において、第2絞り装置18および開閉弁19を制御し、液バックの発生を抑制する点において、実施の形態1と相違する。本実施の形態の冷凍サイクル装置100の冷媒回路構成および制御構成については、図1および図2に示す実施の形態1の冷媒回路構成および制御構成と同様である。
Embodiment 2. FIG.
Next, a second embodiment of the present invention will be described. In the first embodiment, the second expansion device 18 and the on-off valve 19 are controlled in order to suppress the occurrence of liquid back at the start of the defrosting operation. Here, not only at the start of the defrosting operation but also at the end of the defrosting operation, the liquid refrigerant accumulated in the heat source side heat exchanger 13 may return to the compressor 1 to generate a liquid back. Therefore, the second embodiment is different from the first embodiment in that the second throttle device 18 and the on-off valve 19 are controlled at the end of the defrosting operation to suppress the occurrence of liquid back. The refrigerant circuit configuration and the control configuration of the refrigeration cycle apparatus 100 of the present embodiment are the same as the refrigerant circuit configuration and the control configuration of the first embodiment shown in FIGS. 1 and 2.

図4は、本実施の形態における除霜運転終了時の流れを示すフローチャートである。図4に示すように、除霜運転終了条件が成立したか否かが判断され(S21)、除霜運転終了条件が成立していない場合には(S21:NO)、成立するまで除霜運転が継続される。一方、除霜運転終了条件が成立した場合(S21:YES)、開閉弁19が閉じられ(S22)、第2絞り装置18が全開とされる(S23)。これにより、高圧レシーバ16内の圧力が高圧の状態とされる。そして、この状態にて、所定の時間が経過するまで待機する(S24)。このとき、圧縮機11の回転周波数が保持されることで、高圧レシーバ16内に熱源側熱交換器13の液冷媒が溜められる。そして、所定の時間が経過した場合(S24:YES)、流路切替装置12が切り替えられ、除霜運転が終了する(S25)。その後、開閉弁19が開けられ(S26)、加熱運転が再開される。   FIG. 4 is a flowchart showing a flow at the end of the defrosting operation in the present embodiment. As shown in FIG. 4, it is determined whether or not the defrosting operation end condition is satisfied (S21). When the defrosting operation end condition is not satisfied (S21: NO), the defrosting operation is performed until it is satisfied. Will continue. On the other hand, when the defrosting operation end condition is satisfied (S21: YES), the on-off valve 19 is closed (S22), and the second expansion device 18 is fully opened (S23). Thereby, the pressure in the high-pressure receiver 16 is set to a high pressure state. And in this state, it waits until predetermined time passes (S24). At this time, the liquid refrigerant of the heat source side heat exchanger 13 is stored in the high-pressure receiver 16 by maintaining the rotational frequency of the compressor 11. And when predetermined time passes (S24: YES), the flow-path switching apparatus 12 is switched, and a defrost operation is complete | finished (S25). Thereafter, the on-off valve 19 is opened (S26), and the heating operation is resumed.

以上のように、本実施の形態では、除霜運転を終了する条件が成立した場合(S21:YES)であって、除霜運転終了(S25)前に、第2絞り装置18を開け、開閉弁19を閉じることで、熱源側熱交換器13に溜まっていた液冷媒を、高圧レシーバ16に溜める構成となっている。これにより、除霜運転終了時に、熱源側熱交換器13に溜まっていた液冷媒が圧縮機11に液バックすることが抑制される。 As described above, in the present embodiment, when the condition for ending the defrosting operation is satisfied (S21: YES), the second expansion device 18 is opened and opened / closed before the end of the defrosting operation (S25). By closing the valve 19, the liquid refrigerant stored in the heat source side heat exchanger 13 is stored in the high-pressure receiver 16. Thereby, at the end of the defrosting operation, the liquid refrigerant that has accumulated in the heat source side heat exchanger 13 is suppressed from returning to the compressor 11.

以上が本発明の実施の形態の説明であるが、本発明は、上記実施の形態の構成に限定されるものではなく、その技術的思想の範囲内で様々な変形または組み合わせが可能である。例えば、上記実施の形態では、図1に示すように、冷凍サイクル装置100は、1台の圧縮機11、熱源側熱交換器13および利用側熱交換器17を備える場合について説明するが、これらの台数を特に限定するものではない。例えば、2台以上の圧縮機11、熱源側熱交換器13および利用側熱交換器17を備えてもよい。また、上記実施の形態では、冷凍サイクル装置100が水を冷却および加熱して冷水および温水を生成する空冷式ヒートポンプチラーである場合を例に挙げて説明したが、これに限定されず、屋内の冷房および暖房に使用される空気調和装置に本発明を適用してもよい。   The above is the description of the embodiment of the present invention. However, the present invention is not limited to the configuration of the above embodiment, and various modifications or combinations are possible within the scope of the technical idea. For example, in the above embodiment, as shown in FIG. 1, the refrigeration cycle apparatus 100 will be described with respect to a case where it includes one compressor 11, a heat source side heat exchanger 13 and a use side heat exchanger 17. There is no particular limitation on the number of units. For example, two or more compressors 11, the heat source side heat exchanger 13, and the use side heat exchanger 17 may be provided. In the above embodiment, the case where the refrigeration cycle apparatus 100 is an air-cooled heat pump chiller that cools and heats water to generate cold water and hot water has been described as an example. The present invention may be applied to an air conditioner used for cooling and heating.

また、上記実施の形態では、入口温度センサ32および出口温度センサ33によって検出された冷媒温度に基づいて、吸入過熱度制御および過冷却度制御が行われる構成としたが、これに限定されるものではなく、その他の温度センサまたは圧力センサに基づいて吸入過熱度制御および過冷却度制御を行ってもよい。また、吸入過熱度制御および過冷却度制御だけでなく、吐出過熱度制御など、その他の制御を行ってもよい。また、除霜運転開始条件および除霜運転終了条件についても、上記実施の形態に記載されるものに限定されるものではなく、その他の条件を用いてもよい。   In the above embodiment, the intake superheat degree control and the supercool degree control are performed based on the refrigerant temperatures detected by the inlet temperature sensor 32 and the outlet temperature sensor 33. However, the present invention is not limited to this. Instead, suction superheat degree control and supercooling degree control may be performed based on other temperature sensors or pressure sensors. In addition to the suction superheat degree control and the supercooling degree control, other controls such as discharge superheat degree control may be performed. Further, the defrosting operation start condition and the defrosting operation end condition are not limited to those described in the above embodiment, and other conditions may be used.

また、上記実施の形態1および実施の形態2における液バック抑制のための制御は、いずれか一方のみを実施しても良く、また除霜運転開始時および除霜運転終了時の両方に実施しても良い。さらに、本発明の液バック抑制回路40を備えることで、除霜運転時以外にも低外気温下での加熱(暖房)運転終了時など、熱源側熱交換器13に液冷媒が溜まっている状態で、次回起動時において発生し得る液バックを抑制することができる。この場合は、実施の形態2における除霜運転終了時と同様に、加熱運転の終了前に、第2絞り装置18と開閉弁19とを開けて、熱源側熱交換器13に溜まっていた液冷媒を、高圧レシーバ16に溜める。これにより、次回起動時に、熱源側熱交換器13に溜まっていた液冷媒が圧縮機11に液バックすることが抑制される。   Further, the control for suppressing the liquid back in the first embodiment and the second embodiment may be performed only at one of them, or at both the start of the defrosting operation and the end of the defrosting operation. May be. Furthermore, by providing the liquid back suppression circuit 40 of the present invention, liquid refrigerant is accumulated in the heat source side heat exchanger 13 such as at the end of the heating (heating) operation at a low outside temperature other than during the defrosting operation. In this state, liquid back that can occur at the next start-up can be suppressed. In this case, similarly to the end of the defrosting operation in the second embodiment, the liquid that has accumulated in the heat source side heat exchanger 13 by opening the second expansion device 18 and the on-off valve 19 before the end of the heating operation. The refrigerant is stored in the high-pressure receiver 16. As a result, the liquid refrigerant that has accumulated in the heat source side heat exchanger 13 at the next start-up is suppressed from returning to the compressor 11.

1、11 圧縮機、2 四方弁、3 空気熱交換器、4、14 ファン、5 膨張弁、6、16 高圧レシーバ、7 水熱交換器、12 流路切替装置、13 熱源側熱交換器、14 ファン、15 第1絞り装置、17 利用側熱交換器、18 第2絞り装置、19 開閉弁、20 制御部、31 熱交温度センサ、32 入口温度センサ、33 出口温度センサ、34 外気温度センサ、40 液バック抑制回路、100、200 冷凍サイクル装置。   1, 11 Compressor, 2 Four-way valve, 3 Air heat exchanger, 4, 14 Fan, 5 Expansion valve, 6, 16 High pressure receiver, 7 Water heat exchanger, 12 Channel switching device, 13 Heat source side heat exchanger, 14 Fan, 15 1st throttle device, 17 User side heat exchanger, 18 Second throttle device, 19 On-off valve, 20 Control unit, 31 Heat exchange temperature sensor, 32 Inlet temperature sensor, 33 Outlet temperature sensor, 34 Outside air temperature sensor , 40 Liquid back suppression circuit, 100, 200 Refrigeration cycle apparatus.

Claims (3)

圧縮機、流路切替装置、熱源側熱交換器、第1絞り装置および利用側熱交換器を含む冷媒回路と、
第2絞り装置、開閉弁および前記第2絞り装置と前記開閉弁との間に接続される高圧レシーバを含み、前記第1絞り装置に並列に接続される液バック抑制回路と、
前記第2絞り装置および前記開閉弁を制御する制御部と、を備え、
前記制御部は、除霜運転開始条件が成立した場合、前記第2絞り装置および前記開閉弁を閉じ、その後、前記流路切替装置を切り替えて除霜運転を開始するものである冷凍サイクル装置。
A refrigerant circuit including a compressor, a flow path switching device, a heat source side heat exchanger, a first expansion device and a use side heat exchanger;
A liquid back suppression circuit including a second throttling device, an on-off valve and a high-pressure receiver connected between the second throttling device and the on-off valve, and connected in parallel to the first throttling device;
A control unit for controlling the second throttle device and the on-off valve ;
When the defrosting operation start condition is satisfied, the control unit closes the second expansion device and the on-off valve, and then switches the flow path switching device to start the defrosting operation .
前記制御部は、前記除霜運転を開始した後に、前記圧縮機の吸入過熱度が予め定められた値より大きくなった場合に、前記第2絞り装置および前記開閉弁を開けるものである請求項に記載の冷凍サイクル装置。 The control unit is configured to open the second expansion device and the on-off valve when an intake superheat degree of the compressor becomes larger than a predetermined value after starting the defrosting operation. refrigeration cycle apparatus according to 1. 前記制御部は、除霜運転終了条件が成立した場合に、前記第2絞り装置を開け、前記開閉弁を閉じ、その後、前記流路切替装置を切り替えて除霜運転を終了するものである請求項1または2に記載の冷凍サイクル装置。 Wherein, when the defrosting operation end condition is satisfied, opening the second throttle device, closing the on-off valve, then, is to terminate the defrosting operation by switching the flow switching device according Item 3. The refrigeration cycle apparatus according to Item 1 or 2 .
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