JP2007147211A - Control method for refrigerating cycle device and refrigerating cycle device using the same - Google Patents

Control method for refrigerating cycle device and refrigerating cycle device using the same Download PDF

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JP2007147211A
JP2007147211A JP2005345487A JP2005345487A JP2007147211A JP 2007147211 A JP2007147211 A JP 2007147211A JP 2005345487 A JP2005345487 A JP 2005345487A JP 2005345487 A JP2005345487 A JP 2005345487A JP 2007147211 A JP2007147211 A JP 2007147211A
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expansion mechanism
rotation speed
heat exchanger
target
temperature
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JP4665736B2 (en
JP2007147211A5 (en
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Noriho Okaza
典穂 岡座
Kazuo Nakatani
和生 中谷
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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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
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/06Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point using expanders
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • 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
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/06Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F25B2309/061Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
    • 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
    • F25B2339/00Details of evaporators; Details of condensers
    • F25B2339/04Details of condensers
    • F25B2339/047Water-cooled condensers
    • 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
    • F25B2400/14Power generation using energy from the expansion of the refrigerant
    • F25B2400/141Power generation using energy from the expansion of the refrigerant the extracted power is not recycled back in the refrigerant circuit
    • 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
    • F25B2600/025Compressor control by controlling speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2106Temperatures of fresh outdoor air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2115Temperatures of a compressor or the drive means therefor
    • F25B2700/21152Temperatures of a compressor or the drive means therefor at the discharge side of the compressor
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • 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
    • F25B2700/2116Temperatures of a condenser
    • F25B2700/21161Temperatures of a condenser of the fluid heated by the condenser
    • 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
    • F25B9/00Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/002Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
    • F25B9/008Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide

Abstract

<P>PROBLEM TO BE SOLVED: To stabilize operation of a refrigerating cycle device equipped with an expansion mechanism capable of recovering pressure energy at the time of expansion, and especially, to improve stability at the start of its operation. <P>SOLUTION: The refrigerating cycle device is equipped with a compression mechanism 2, a heat-source-side heat exchanger 6, the expansion mechanism for recovering power, and a use-side heat exchanger 3. The method for controlling the refrigerating cycle device is characterized to control the rotating speed of the expansion mechanism 5 so as to become a first target expansion mechanism rotating speed determined from the discharge temperature of the compression mechanism 2. With the method, the rotating speed of the expansion mechanism 5 can be suitably controlled and the refrigerating cycle device can be stably operated, and especially, the stability at start of the operation of the refrigerating cycle can be improved. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、動力を回収する膨張機構を備えた冷凍サイクル装置の制御方法およびそれを用いた冷凍サイクル装置に関する。   The present invention relates to a control method for a refrigeration cycle apparatus having an expansion mechanism for recovering power and a refrigeration cycle apparatus using the same.

減圧器の代わりに膨張機構を設けて、膨張時の圧力エネルギーを動力として回収し、COPを向上させる冷凍サイクル装置が提案されている(例えば特許文献1参照)。
特開昭56−112896号公報
A refrigeration cycle apparatus has been proposed in which an expansion mechanism is provided instead of a decompressor, and pressure energy at the time of expansion is recovered as power to improve COP (see, for example, Patent Document 1).
JP-A-56-112896

上記、従来技術では、熱源側熱交換器に流入する熱源側流体の温度や利用側熱交換器に流入する利用側流体の温度が高い場合には、圧縮機構の吐出温度や高圧側圧力が上昇しやすく、機器を保護するために圧縮機構の運転を停止することが頻繁に起こるといった課題が生じていた。   In the above prior art, when the temperature of the heat source side fluid flowing into the heat source side heat exchanger or the temperature of the usage side fluid flowing into the usage side heat exchanger is high, the discharge temperature and the high pressure side pressure of the compression mechanism rise. There is a problem that the operation of the compression mechanism is frequently stopped to protect the device.

そこで、本発明は、上記課題を解決するため、膨張機構を備えた冷凍サイクル装置において、適切に膨張機構の回転数を制御し、冷凍サイクル装置を安定して運転させることを目的とし、特に、冷凍サイクル装置の起動時の安定性を向上させることを目的とする。   Then, in order to solve the above-mentioned problem, the present invention aims to control the rotation speed of the expansion mechanism appropriately in the refrigeration cycle apparatus provided with the expansion mechanism and to operate the refrigeration cycle apparatus stably. It aims at improving the stability at the time of starting of a refrigerating cycle device.

前記従来の課題を解決するために、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御するものである。これによると、吐出温度が目標吐出温度から大きく外れることがないため、冷凍サイクル装置を保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。 In order to solve the above-described conventional problems, a control method for a refrigeration cycle apparatus according to the present invention includes a first target expansion mechanism rotational speed determined from a discharge temperature of a compression mechanism in a refrigeration cycle apparatus including an expansion mechanism that performs power recovery. Thus, the rotational speed of the expansion mechanism is controlled. According to this, since the discharge temperature does not greatly deviate from the target discharge temperature, it is not necessary to stop the operation of the compression mechanism or the like in order to protect the refrigeration cycle apparatus, and the refrigeration cycle apparatus can be operated stably. .

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、圧縮機構の吐出温度が、予め定められた目標吐出温度より高い場合には、膨張機構の回転数を増加させ、目標吐出温度より低い場合には、膨張機構の回転数を低下させるものである。これによると、吐出温度が目標吐出温度を越える場合には、膨張機構の回転数を増加させ、吐出温度を下げるようにし、吐出温度が目標吐出温度を下回る場合には、膨張機構の回転数を低下させ、吐出温度を上げるようにするので、吐出温度が目標吐出温度から大きく外れることがないため、冷凍サイクル装置を保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   In the refrigeration cycle apparatus control method of the present invention, in the refrigeration cycle apparatus provided with an expansion mechanism for recovering power, when the discharge temperature of the compression mechanism is higher than a predetermined target discharge temperature, the expansion mechanism When the rotational speed is increased and lower than the target discharge temperature, the rotational speed of the expansion mechanism is decreased. According to this, when the discharge temperature exceeds the target discharge temperature, the rotation speed of the expansion mechanism is increased and the discharge temperature is decreased, and when the discharge temperature is lower than the target discharge temperature, the rotation speed of the expansion mechanism is decreased. Since the discharge temperature does not deviate greatly from the target discharge temperature because the discharge temperature is lowered and the discharge temperature is increased, it is not necessary to stop the operation of the compression mechanism or the like in order to protect the refrigeration cycle device, and the refrigeration can be stably performed. The cycle device can be operated.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の上限値を超える場合には、圧縮機構の回転数を低下させるものである。これによると、吐出温度が目標吐出温度より高い場合で、膨張機構の回転数が使用上限回転数より大きい場合であっても、圧縮機構の回転数を減少させ、吐出温度を下げるようにするので、膨張機構などを保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   In the refrigeration cycle apparatus control method according to the present invention, in the refrigeration cycle apparatus having an expansion mechanism for recovering power, the rotation speed of the expansion mechanism exceeds a predetermined upper limit value of the use range of the rotation speed of the expansion mechanism. In this case, the rotational speed of the compression mechanism is reduced. According to this, even when the discharge temperature is higher than the target discharge temperature and the rotation speed of the expansion mechanism is higher than the upper limit rotation speed, the rotation speed of the compression mechanism is decreased and the discharge temperature is lowered. In addition, it is not necessary to stop the operation of the compression mechanism in order to protect the expansion mechanism and the like, and the refrigeration cycle apparatus can be stably operated.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍
サイクル装置において、膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の下限値を超える場合には、圧縮機構の回転数を増加させるものである。これによると吐出温度が目標吐出温度より低い場合で、膨張機構の回転数が使用下限回転数より小さい場合であっても、圧縮機構の回転数を増加させ、吐出温度を上げるようにするので、膨張機構などを保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。
In the refrigeration cycle apparatus control method according to the present invention, in the refrigeration cycle apparatus including an expansion mechanism that performs power recovery, the rotation speed of the expansion mechanism exceeds a lower limit value of a predetermined use range of the rotation speed of the expansion mechanism. In this case, the rotational speed of the compression mechanism is increased. According to this, even when the discharge temperature is lower than the target discharge temperature and the rotation speed of the expansion mechanism is smaller than the lower limit rotation speed of use, the rotation speed of the compression mechanism is increased and the discharge temperature is increased. There is no need to stop the operation of the compression mechanism or the like to protect the expansion mechanism or the like, and the refrigeration cycle apparatus can be stably operated.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、圧縮機構の回転数を変更すると同時、あるいは、変更する前に、膨張機構の回転数を変更するものである。これによると、圧縮機構の回転数が変化する際の急激な高圧側圧力の変化を防止でき、安定した冷凍サイクル装置の起動が実現できる。   Further, according to the control method of the refrigeration cycle apparatus of the present invention, in the refrigeration cycle apparatus having an expansion mechanism for recovering power, the rotation speed of the expansion mechanism is changed at the same time as or before the rotation speed of the compression mechanism is changed. To change. According to this, a rapid change in the high-pressure side pressure when the rotation speed of the compression mechanism changes can be prevented, and a stable start-up of the refrigeration cycle apparatus can be realized.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持するものである。これによると、第2目標膨張機構回転数は外気温度、入水温度に応じて、高圧側圧力が上昇しやすい状態ほど、回転数が大きくなるように設定されているので、急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   The control method for the refrigeration cycle apparatus according to the present invention includes a heat source side fluid temperature flowing into the heat source side heat exchanger and a utilization side flowing into the utilization side heat exchanger in the refrigeration cycle apparatus having an expansion mechanism for performing power recovery. The rotation speed of the expansion mechanism is maintained for a predetermined time at the second target expansion mechanism rotation speed determined from at least one of the fluid temperatures. According to this, the second target expansion mechanism rotational speed is set so that the rotational speed increases as the high-pressure side pressure easily rises according to the outside air temperature and the incoming water temperature. The rise can be prevented, and a stable refrigeration cycle apparatus can be started.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、少なくとも圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御するものである。これによると、第2目標膨張機構回転数は外気温度、入水温度に応じて、高圧側圧力が上昇しやすい状態ほど、回転数が大きくなるように設定されているので、膨張機構の回転数が第1目標膨張機構回転数へと増加する際に、急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   The control method for the refrigeration cycle apparatus according to the present invention includes a heat source side fluid temperature flowing into the heat source side heat exchanger and a utilization side flowing into the utilization side heat exchanger in the refrigeration cycle apparatus having an expansion mechanism for performing power recovery. The second target expansion mechanism rotation speed determined from at least one of the fluid temperatures is maintained at the rotation speed of the expansion mechanism for a predetermined time, and after the predetermined time has elapsed, the first target expansion determined from at least the discharge temperature of the compression mechanism. The rotation speed of the expansion mechanism is controlled so as to be the mechanism rotation speed. According to this, the second target expansion mechanism rotation speed is set so that the rotation speed increases as the pressure on the high pressure side increases more easily according to the outside air temperature and the incoming water temperature. When the rotation speed increases to the first target expansion mechanism rotation speed, a rapid increase in the high-pressure side pressure can be prevented, and stable start-up of the refrigeration cycle apparatus can be realized.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第3目標膨張機構回転数に、膨張機構の回転数を制御し、さらに所定経過後、少なくとも圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御するものである。これによると、膨張機構の回転数が、第2目標膨張機構回転数から第1目標膨張機構回転数へと増加する際の急激な高圧側圧力の変化を防止でき、起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   The control method for the refrigeration cycle apparatus according to the present invention includes a heat source side fluid temperature flowing into the heat source side heat exchanger and a utilization side flowing into the utilization side heat exchanger in the refrigeration cycle apparatus having an expansion mechanism for performing power recovery. The second target expansion mechanism rotation speed determined from at least one of the fluid temperatures is maintained at the rotation speed of the expansion mechanism for a predetermined time, and after the predetermined time has elapsed, the heat source side fluid temperature flowing into the heat source side heat exchanger, The rotation speed of the expansion mechanism is controlled to a third target expansion mechanism rotation speed determined from at least one temperature of the use-side fluid temperature flowing into the use-side heat exchanger, and after a predetermined elapse, at least from the discharge temperature of the compression mechanism The rotation speed of the expansion mechanism is controlled so as to be the first target expansion mechanism rotation speed to be determined. According to this, it is possible to prevent a rapid change in the high-pressure side pressure when the rotation speed of the expansion mechanism increases from the second target expansion mechanism rotation speed to the first target expansion mechanism rotation speed, and to stabilize while reducing the start-up time. The refrigeration cycle apparatus can be started up.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、圧縮機構の吐出温度が予め定められた目標吐出温度に近づけば、所定時間を終了したと判定するものである。これによると、不必要に低い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   In the refrigeration cycle apparatus control method of the present invention, in the refrigeration cycle apparatus provided with an expansion mechanism for recovering power, if the discharge temperature of the compression mechanism approaches a predetermined target discharge temperature, the predetermined time is ended. Judgment. According to this, it is possible to shorten the time required for operation at an unnecessarily low target expansion mechanism rotation speed, and it is possible to realize stable start-up of the refrigeration cycle apparatus while shortening the start-up time.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、利用側熱交換器に流入する利用側流体温度が予め定められた目標温度に近づけば、所定時間を終了したと判定するものである。これによると、不必要に低
い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。
In the refrigeration cycle apparatus according to the present invention, the refrigeration cycle apparatus including the expansion mechanism that performs power recovery, if the use side fluid temperature flowing into the use side heat exchanger approaches a predetermined target temperature, It is determined that the predetermined time has ended. According to this, it is possible to shorten the time required for operation at an unnecessarily low target expansion mechanism rotation speed, and it is possible to realize stable start-up of the refrigeration cycle apparatus while shortening the start-up time.

また、本発明の冷凍サイクル装置の制御方法は、動力回収を行う膨張機構を備えた冷凍サイクル装置において、圧縮機構の吐出温度が予め定められた前記利用側熱交換器に流入する利用側流体温度の目標温度よりある一定温度差以上高くなれば、所定時間を終了したと判定するものである。これによると、不必要に低い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   In the refrigeration cycle apparatus control method according to the present invention, in the refrigeration cycle apparatus having an expansion mechanism for recovering power, the use side fluid temperature at which the discharge temperature of the compression mechanism flows into the predetermined use side heat exchanger is determined. If the predetermined temperature difference is higher than the target temperature by a certain temperature, it is determined that the predetermined time has ended. According to this, it is possible to shorten the time required for operation at an unnecessarily low target expansion mechanism rotation speed, and it is possible to realize stable start-up of the refrigeration cycle apparatus while shortening the start-up time.

また、本発明の冷凍サイクル装置は、上記制御方法を行う冷凍サイクル装置である。これによると、安定した起動、および、運転をおこなうことが可能な冷凍サイクル装置が実現できる。   Moreover, the refrigerating cycle apparatus of this invention is a refrigerating cycle apparatus which performs the said control method. According to this, it is possible to realize a refrigeration cycle apparatus capable of performing stable start-up and operation.

また、本発明の冷凍サイクル装置は、冷媒が二酸化炭素である。この場合には高圧側圧力が上昇しやすく、安定した冷凍サイクル装置の運転が実現できる効果が、特に大きい。   In the refrigeration cycle apparatus of the present invention, the refrigerant is carbon dioxide. In this case, the high pressure side pressure is likely to increase, and the effect of realizing a stable operation of the refrigeration cycle apparatus is particularly great.

本発明の冷凍サイクル装置の制御方法およびそれを用いた冷凍サイクル装置は、膨張機構を備えた冷凍サイクル装置において、適切に膨張機構の回転数を制御し、冷凍サイクル装置を安定して運転させることが可能であり、特に、冷凍サイクル装置の起動時の安定性を向上させることができる。   A control method for a refrigeration cycle apparatus according to the present invention and a refrigeration cycle apparatus using the same, in a refrigeration cycle apparatus provided with an expansion mechanism, appropriately control the number of rotations of the expansion mechanism and stably operate the refrigeration cycle apparatus. In particular, it is possible to improve the stability at the start-up of the refrigeration cycle apparatus.

第1の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御することにより、吐出温度が目標吐出温度から大きく外れることがないため、冷凍サイクル装置を保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   A first invention is a refrigeration cycle apparatus having a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, and a first target expansion mechanism rotational speed determined from a discharge temperature of the compression mechanism By controlling the rotation speed of the expansion mechanism so that the discharge temperature does not greatly deviate from the target discharge temperature, it is not necessary to stop the operation of the compression mechanism or the like to protect the refrigeration cycle device, The refrigeration cycle apparatus can be operated stably.

第2の発明は、第1の発明において、特に、圧縮機構の吐出温度が、予め定められた目標吐出温度より高い場合には、膨張機構の回転数を増加させ、目標吐出温度より低い場合には、膨張機構の回転数を低下させることにより、吐出温度が目標吐出温度を高い場合には、膨張機構の回転数を増加させ、吐出温度を下げるようにし、吐出温度が目標吐出温度を低い場合には、膨張機構の回転数を低下させ、吐出温度を上げるようにするので、吐出温度が目標吐出温度から大きく外れることがないため、冷凍サイクル装置を保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   According to a second invention, in the first invention, in particular, when the discharge temperature of the compression mechanism is higher than a predetermined target discharge temperature, the number of rotations of the expansion mechanism is increased and is lower than the target discharge temperature. If the discharge temperature is higher than the target discharge temperature by reducing the rotation speed of the expansion mechanism, the rotation speed of the expansion mechanism is increased to lower the discharge temperature, and the discharge temperature is lower than the target discharge temperature. In order to protect the refrigeration cycle device, the operation of the compression mechanism is stopped because the rotation speed of the expansion mechanism is decreased and the discharge temperature is raised so that the discharge temperature does not deviate significantly from the target discharge temperature. Therefore, the refrigeration cycle apparatus can be stably operated.

第3の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、吐出温度が目標吐出温度より高い場合であって、膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の上限値を超える場合には、圧縮機構の回転数を低下させることにより、膨張機構の回転数が使用上限回転数より大きい場合であっても、吐出温度を下げることができるので、膨張機構などを保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   A third invention is a refrigeration cycle apparatus having a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, wherein the discharge temperature is higher than the target discharge temperature, and the expansion mechanism When the rotation speed of the expansion mechanism exceeds the upper limit value of the use range of the rotation speed of the expansion mechanism, the rotation speed of the expansion mechanism is decreased to reduce the rotation speed of the expansion mechanism. Even if it exists, since discharge temperature can be lowered | hung, in order to protect an expansion mechanism etc., it is not necessary to stop operation | movement of a compression mechanism etc., and a refrigerating-cycle apparatus can be operated stably.

第4の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、吐出温度が目標吐出温度より低い場合であって、膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の下限値を超える場合には
、圧縮機構の回転数を増加させることにより、膨張機構の回転数が使用下限回転数より小さい場合であっても、吐出温度を上げることができるので、膨張機構などを保護するために圧縮機構などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。
A fourth invention is a refrigeration cycle apparatus having a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, wherein the discharge temperature is lower than the target discharge temperature, and the expansion mechanism If the rotation speed of the expansion mechanism exceeds the lower limit value of the predetermined use range of the rotation speed of the expansion mechanism, the rotation speed of the expansion mechanism is increased so that the rotation speed of the expansion mechanism is smaller than the lower limit rotation speed of use. Even if it exists, since discharge temperature can be raised, it is not necessary to stop operation | movement of a compression mechanism etc. in order to protect an expansion mechanism etc., and a refrigerating-cycle apparatus can be operated stably.

第5の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、圧縮機構の回転数を変更すると同時、あるいは、変更する前に、膨張機構の回転数を変更することにより、圧縮機構の回転数が変化する際の急激な高圧側圧力の変化を防止でき、安定した冷凍サイクル装置の起動が実現できる。   5th invention is a refrigerating-cycle apparatus provided with the compression mechanism, the heat source side heat exchanger, the expansion mechanism which performs motive power recovery, and the utilization side heat exchanger, at the same time as changing the rotation speed of the compression mechanism or before changing In addition, by changing the rotation speed of the expansion mechanism, it is possible to prevent a rapid change in the high-pressure side pressure when the rotation speed of the compression mechanism changes, and to realize stable start-up of the refrigeration cycle apparatus.

第6の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置の起動時の制御方法であって、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持するものである。第2目標膨張機構回転数は外気温度、入水温度に応じて、高圧側圧力が上昇しやすい状態ほど、回転数が大きくなるように設定されているので、急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   6th invention is a control method at the time of starting of a refrigerating cycle device provided with a compression mechanism, a heat source side heat exchanger, an expansion mechanism which performs power recovery, and a use side heat exchanger, and flows into the heat source side heat exchanger The rotation speed of the expansion mechanism is maintained for a predetermined time at the second target expansion mechanism rotation speed determined from at least one of the heat source side fluid temperature and the utilization side fluid temperature flowing into the utilization side heat exchanger. The second target expansion mechanism rotation speed is set so that the higher the high pressure side pressure is, the higher the rotation speed is, depending on the outside air temperature and the incoming water temperature. A stable refrigeration cycle apparatus can be activated.

第7の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、少なくとも圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御するものである。第2目標膨張機構回転数は外気温度、入水温度に応じて、高圧側圧力が上昇しやすい状態ほど、回転数が大きくなるように設定されているので、膨張機構の回転数が第1目標膨張機構回転数へと増加する際に、急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   7th invention is a refrigerating cycle device provided with a compression mechanism, a heat source side heat exchanger, an expansion mechanism which performs power recovery, and a use side heat exchanger, heat source side fluid temperature and use side which flow into a heat source side heat exchanger Maintaining the rotation speed of the expansion mechanism for a predetermined time to the second target expansion mechanism rotation speed determined from at least one of the use-side fluid temperatures flowing into the heat exchanger, and further discharging at least the compression mechanism after a predetermined time has elapsed. The rotational speed of the expansion mechanism is controlled so as to be the first target expansion mechanism rotational speed determined from the temperature. The second target expansion mechanism rotational speed is set so that the rotational speed increases as the pressure on the high pressure side increases more easily according to the outside air temperature and the incoming water temperature. When the rotational speed increases to the mechanism rotational speed, it is possible to prevent a rapid increase in the high-pressure side pressure and to realize a stable start-up of the refrigeration cycle apparatus.

第8の発明は、圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、熱源側熱交換器に流入する熱源側流体温度と利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第3目標膨張機構回転数に、膨張機構の回転数を制御し、さらに所定経過後、少なくとも圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、膨張機構の回転数を制御するものであり、膨張機構の回転数が、第2目標膨張機構回転数から第1目標膨張機構回転数へと増加する際の急激な高圧側圧力の変化を防止でき、起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   An eighth invention is a refrigeration cycle apparatus including a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, and the heat source side fluid temperature flowing into the heat source side heat exchanger and the use side Maintaining the rotation speed of the expansion mechanism for a predetermined time to the second target expansion mechanism rotation speed determined from at least one of the use-side fluid temperatures flowing into the heat exchanger, and after a predetermined time has elapsed, the heat source side heat exchanger The rotation speed of the expansion mechanism is controlled to a third target expansion mechanism rotation speed determined from at least one of the heat source side fluid temperature flowing into the heat source side and the utilization side fluid temperature flowing into the utilization side heat exchanger. The rotation speed of the expansion mechanism is controlled so as to be at least the first target expansion mechanism rotation speed determined from the discharge temperature of the compression mechanism. The rotation speed of the expansion mechanism is the second target expansion mechanism rotation speed from the second target expansion mechanism rotation speed. 1 target expansion mechanism It prevents sudden changes in the high-pressure side pressure when increases to rotation number, activation of the stable refrigerating cycle device can be realized while reducing the boot time.

第9の発明は、第6〜8のいずれかの発明において、特に、圧縮機構の吐出温度が予め定められた目標吐出温度に近づけば、所定時間を終了したと判定するものであり、不必要に低い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   According to a ninth aspect of the present invention, in any one of the sixth to eighth aspects, it is determined that the predetermined time has ended, particularly if the discharge temperature of the compression mechanism approaches a predetermined target discharge temperature. In addition, it is possible to shorten the time for operation at a low target expansion mechanism rotation speed, and to realize stable start-up of the refrigeration cycle apparatus while further shortening the start-up time.

第10の発明は、第6〜8のいずれかの発明において、特に、利用側熱交換器に流入する利用側流体温度が予め定められた目標温度に近づけば、所定時間を終了したと判定するものであり、不必要に低い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   According to a tenth aspect of the present invention, in any of the sixth to eighth aspects of the invention, in particular, if the use side fluid temperature flowing into the use side heat exchanger approaches a predetermined target temperature, it is determined that the predetermined time has ended. Therefore, it is possible to shorten the time for operation at an unnecessarily low target expansion mechanism rotation speed, and to realize stable start-up of the refrigeration cycle apparatus while further shortening the start-up time.

第11の発明は、第6〜8のいずれかの発明において、特に、圧縮機構の吐出温度が予
め定められた利用側熱交換器に流入する利用側流体温度の目標温度よりある一定温度差以上高くなれば、前記所定時間を終了したと判定するものであり、不必要に低い目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。
In an eleventh aspect of the invention according to any one of the sixth to eighth aspects, in particular, the discharge temperature of the compression mechanism is equal to or greater than a certain temperature difference from a target temperature of the use side fluid temperature flowing into the predetermined use side heat exchanger. If it becomes higher, it is determined that the predetermined time has ended, the time required for operation at an unnecessarily low target expansion mechanism rotational speed can be shortened, and the start-up of the refrigeration cycle apparatus can be stabilized while reducing the start-up time. realizable.

第12の発明は、第1〜11のいずれかの発明の制御方法を用いた冷凍サイクル装置であり、安定した起動、および、運転をおこなうことが可能な冷凍サイクル装置が実現できる。   The twelfth invention is a refrigeration cycle apparatus using the control method of any one of the first to eleventh inventions, and can realize a refrigeration cycle apparatus capable of performing stable start-up and operation.

第13の発明は、第12の発明において、特に、冷媒を二酸化炭素としたものであり、この場合には高圧側圧力が上昇しやすく、安定した冷凍サイクル装置の運転が実現できる効果が、特に大きい。   The thirteenth aspect of the invention is that in the twelfth aspect of the invention, in particular, the refrigerant is carbon dioxide. In this case, the high-pressure side pressure is likely to increase, and the effect of realizing a stable operation of the refrigeration cycle apparatus is particularly significant. large.

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。例えば、以下の実施の形態では、給湯機を例にとり説明するが、本発明が給湯機に限定されるものではなく、空気調和機などであってもよい。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments. For example, in the following embodiment, a hot water heater will be described as an example, but the present invention is not limited to the hot water heater, and may be an air conditioner or the like.

(実施の形態1)
本発明の第1の実施の形態における冷凍サイクル装置の制御方法を、図1に概略構成図を示す冷凍サイクル装置を用いて説明する。図1の冷凍サイクル装置は、電動機1により駆動される圧縮機構2、利用側熱交換器としての放熱器3の冷媒流路、発電機4により動力回収される膨張機構5、熱源側熱交換器としての蒸発器6などからなり、冷媒として例えばCO冷媒が封入されている冷媒回路Aと、利用流体搬送手段としての給水ポンプ7、放熱器3の流体流路、および給湯タンク8などからなる流体回路Bとから構成されている。
(Embodiment 1)
A control method for the refrigeration cycle apparatus according to the first embodiment of the present invention will be described with reference to the refrigeration cycle apparatus schematically shown in FIG. The refrigeration cycle apparatus of FIG. 1 includes a compression mechanism 2 driven by an electric motor 1, a refrigerant flow path of a radiator 3 as a use side heat exchanger, an expansion mechanism 5 that recovers power by a generator 4, and a heat source side heat exchanger. For example, a refrigerant circuit A in which a CO 2 refrigerant is enclosed as a refrigerant, a water supply pump 7 as a utilization fluid conveying means, a fluid flow path of the radiator 3, a hot water supply tank 8, and the like. And a fluid circuit B.

さらに、この冷凍サイクル装置は熱源流体搬送手段としての送風装置9を備えており、送風装置9は、蒸発器6に熱源流体(例えば、外気)を送風する。また、電動機1の回転数を制御する圧縮機構制御手段10、発電機4の回転数を制御する膨張機構制御手段11を備えている。膨張機構制御手段11により、冷凍サイクルの状態に応じて膨張機構5の回転数を適切に変更し、例えば、高圧側圧力、吐出温度などを変更することができる。   Further, the refrigeration cycle apparatus includes a blower 9 as a heat source fluid transport unit, and the blower 9 blows a heat source fluid (for example, outside air) to the evaporator 6. Further, a compression mechanism control means 10 for controlling the rotational speed of the electric motor 1 and an expansion mechanism control means 11 for controlling the rotational speed of the generator 4 are provided. The expansion mechanism control means 11 can appropriately change the rotation speed of the expansion mechanism 5 according to the state of the refrigeration cycle, for example, the high pressure side pressure, the discharge temperature, and the like.

さらに、吐出温度検知手段12は、圧縮機構2の吐出側から放熱器3の冷媒入口側までの冷媒配管上に備えられており、圧縮機構2の吐出温度を検知する。熱源流体入口温度検知手段としての外気温度検知手段13は、蒸発器6のフィン等に固定されており、蒸発器6に流入する外気の温度を検知する。利用流体温度検知手段としての入水温度検知手段14は、給湯タンク8の底部から放熱器6の流体入口側までの流体配管上に備えられており、放熱器6に流入する利用流体(例えば、水)の温度を検知する。電子制御手段15は、吐出温度検知手段12、外気温度検知手段13、入水温度検知手段14などからの信号により、冷凍サイクルの状態を判断し、圧縮機構制御手段10、膨張機構制御手段11などに指示を与える。   Further, the discharge temperature detection means 12 is provided on the refrigerant pipe from the discharge side of the compression mechanism 2 to the refrigerant inlet side of the radiator 3 and detects the discharge temperature of the compression mechanism 2. The outside air temperature detection means 13 as the heat source fluid inlet temperature detection means is fixed to the fins of the evaporator 6 and detects the temperature of the outside air flowing into the evaporator 6. The incoming water temperature detecting means 14 as the used fluid temperature detecting means is provided on the fluid piping from the bottom of the hot water supply tank 8 to the fluid inlet side of the radiator 6, and the used fluid flowing into the radiator 6 (for example, water ) Is detected. The electronic control means 15 determines the state of the refrigeration cycle based on signals from the discharge temperature detection means 12, the outside air temperature detection means 13, the incoming water temperature detection means 14, and the like, and sends it to the compression mechanism control means 10, the expansion mechanism control means 11 and the like. Give instructions.

次に、上述のように構成された冷凍サイクル装置の動作で、特に、外気温度や入水温度の変化が少ない、あるいは、利用者からの指示がないなど、冷凍サイクルの変化が小さい場合の動作について説明する。冷媒回路Aでは、CO冷媒を、圧縮機構2で臨界圧力を越える圧力まで圧縮する。その圧縮された冷媒は、高温高圧状態となり、放熱器3の冷媒流路を流れる際に、放熱器3の流体流路を流れる水に放熱し冷却される。その後、冷媒は膨張機構5で減圧され低温低圧の気液二相状態となる。膨張機構5で回収された膨張時の圧力エネルギーは、発電機4に伝達され、電力として回収される。 Next, regarding the operation of the refrigeration cycle apparatus configured as described above, particularly when the change in the refrigeration cycle is small, such as a small change in the outside air temperature or the incoming water temperature, or no instruction from the user. explain. In the refrigerant circuit A, the CO 2 refrigerant is compressed by the compression mechanism 2 to a pressure exceeding the critical pressure. The compressed refrigerant becomes a high-temperature and high-pressure state, and when it flows through the refrigerant flow path of the radiator 3, it dissipates heat to the water flowing through the fluid flow path of the radiator 3 and is cooled. Thereafter, the refrigerant is depressurized by the expansion mechanism 5 and becomes a low-temperature low-pressure gas-liquid two-phase state. The pressure energy at the time of expansion recovered by the expansion mechanism 5 is transmitted to the generator 4 and recovered as electric power.

すなわち、膨張時の圧力エネルギーを動力として回収しCOPを向上させることができる。膨張機構5で減圧された冷媒は蒸発器6に供給される。蒸発器6では、冷媒は送風装置9によって送り込まれた外気によって加熱され、気液二相またはガス状態となる。蒸発器6を流出した冷媒は、再び、圧縮機構2に吸入される。一方、流体回路Bでは、給湯タンク8の底部から給水ポンプ7により放熱器3の流体流路へ送り込まれた利用流体(例えば、水)は、放熱器3の冷媒流路を流れる冷媒により加熱され、高温の流体(例えば、お湯)となり、その高温流体を給湯タンク8の頂部から貯める。このようなサイクルを繰り返すことにより、本実施例の冷凍サイクル装置は、給湯機として利用できる。   That is, COP can be improved by recovering pressure energy during expansion as power. The refrigerant decompressed by the expansion mechanism 5 is supplied to the evaporator 6. In the evaporator 6, the refrigerant is heated by the outside air sent by the blower 9, and enters a gas-liquid two-phase or gas state. The refrigerant that has flowed out of the evaporator 6 is again sucked into the compression mechanism 2. On the other hand, in the fluid circuit B, the use fluid (for example, water) sent from the bottom of the hot water supply tank 8 to the fluid flow path of the radiator 3 by the water supply pump 7 is heated by the refrigerant flowing through the refrigerant flow path of the radiator 3. The hot fluid (for example, hot water) is stored, and the hot fluid is stored from the top of the hot water supply tank 8. By repeating such a cycle, the refrigeration cycle apparatus of the present embodiment can be used as a water heater.

次に、制御方法について説明する。圧縮機構2、実質的には駆動源である電動機1は、外気温度検知手段13、入水温度検知手段14などが検知した外気温度や入水温度、利用者等が設定した目標沸上温度(給湯タンクに貯めるお湯の温度、または、放熱器6の流体出口側温度の目標値)などから電子制御装置15が算出した回転数(以降、第1目標圧縮機構回転数と呼ぶ)となるように、圧縮機構制御手段10により制御されている。   Next, a control method will be described. The compression mechanism 2, or the electric motor 1 that is substantially a drive source, includes an outside air temperature detection means 13, an incoming water temperature detection means 14, and the like, a target boiling temperature (a hot water tank) set by a user and the like. Compression so that the rotational speed (hereinafter referred to as the first target compression mechanism rotational speed) calculated by the electronic control unit 15 based on the temperature of hot water stored in the air or the target value of the fluid outlet side temperature of the radiator 6) is obtained. It is controlled by the mechanism control means 10.

また、膨張機構5、実質的には発電機4は、図2に示すフローチャートのように、膨張機構制御手段11により制御されている。電子制御装置15は、外気温度検知手段13、入水温度検知手段14などが検知した外気温度や入水温度、利用者等が設定した沸上温度(給湯タンクに貯めるお湯の温度、または、放熱器6の流体出口側温度)などから、冷凍サイクルの状態が最適となる目標吐出温度Td0を算出する(ステップ100)。   Further, the expansion mechanism 5, substantially the generator 4, is controlled by the expansion mechanism control means 11 as shown in the flowchart of FIG. 2. The electronic control unit 15 uses the outside air temperature detection means 13, the incoming water temperature detection means 14 and the like detected by the outside air temperature, the incoming water temperature, the boiling temperature set by the user (the temperature of hot water stored in the hot water supply tank, or the radiator 6). The target discharge temperature Td0 at which the state of the refrigeration cycle is optimal is calculated from the fluid outlet side temperature) (step 100).

この目標吐出温度Td0は、圧縮機構2などの構成要素の使用温度上限や圧力上限を越えないように設定されている。次に、吐出温度検知手段12により吐出温度Tdを検知する(ステップ110)。検知した吐出温度Tdが目標吐出温度Td0にある一定値ΔT1を加えた値より、大きいか否かを判定する(ステップ120)。なお、ΔT1は、冷凍サイクルの状態の安定性を増すために、吐出温度Tdがある一定の温度範囲となるように加える微少値である。   This target discharge temperature Td0 is set so as not to exceed the use temperature upper limit and pressure upper limit of components such as the compression mechanism 2. Next, the discharge temperature detecting means 12 detects the discharge temperature Td (step 110). It is determined whether or not the detected discharge temperature Td is higher than a value obtained by adding a certain value ΔT1 to the target discharge temperature Td0 (step 120). Note that ΔT1 is a minute value that is added so that the discharge temperature Td falls within a certain temperature range in order to increase the stability of the state of the refrigeration cycle.

ステップ120において、吐出温度TdがTd0+ΔT1より高いと判定された場合には、ステップ130で、膨張機構5の回転数Rexpが、膨張機構5の使用上限回転数Rexp_maxより、大きいか否かを判定する。膨張機構5の使用上限回転数Rexp_maxは、膨張機構5や膨張機構制御手段11の保護するための上限値として設定されている。ステップ130において、膨張機構5の回転数Rexpが、使用上限回転数Rexp_maxより小さいと判定された場合には、膨張機構5、および、発電機4の回転数をある一定量、増加させるように膨張機構制御手段11に指示する(ステップ140)。これにより、膨張機構5を流通する冷媒量が増加するため、吐出温度Tdや高圧側圧力を低下させることができる。   If it is determined in step 120 that the discharge temperature Td is higher than Td0 + ΔT1, it is determined in step 130 whether or not the rotation speed Reexp of the expansion mechanism 5 is higher than the upper limit rotation speed Reexp_max of the expansion mechanism 5. . The upper limit rotation speed Reexp_max of the expansion mechanism 5 is set as an upper limit value for protecting the expansion mechanism 5 and the expansion mechanism control means 11. If it is determined in step 130 that the rotation speed Reexp of the expansion mechanism 5 is smaller than the upper limit rotation speed Reexp_max, the expansion is performed so that the rotation speed of the expansion mechanism 5 and the generator 4 is increased by a certain amount. The mechanism control means 11 is instructed (step 140). Thereby, since the refrigerant | coolant amount which distribute | circulates the expansion mechanism 5 increases, discharge temperature Td and a high voltage | pressure side pressure can be reduced.

ステップ120において、吐出温度TdがTd0+ΔT1より低いと判定された場合には、ステップ150で、吐出温度Tdが目標吐出温度Td0よりある一定値ΔT2を減じた値より、小さいか否かを判定する。なお、ΔT2は、冷凍サイクルの状態の安定性を増すために、吐出温度Tdがある一定の温度範囲となるように減じる微少値である。ステップ150において、吐出温度TdがTd0−ΔT2より低いと判定された場合には、ステップ160で、膨張機構5の回転数Rexpが、膨張機構5の使用下限回転数Rexp_minより、小さいか否かを判定する。   If it is determined in step 120 that the discharge temperature Td is lower than Td0 + ΔT1, it is determined in step 150 whether or not the discharge temperature Td is smaller than a value obtained by subtracting a certain value ΔT2 from the target discharge temperature Td0. Note that ΔT2 is a minute value that is decreased so that the discharge temperature Td falls within a certain temperature range in order to increase the stability of the state of the refrigeration cycle. If it is determined in step 150 that the discharge temperature Td is lower than Td0−ΔT2, it is determined in step 160 whether or not the rotation speed Reexp of the expansion mechanism 5 is smaller than the lower limit rotation speed Reexp_min of the expansion mechanism 5. judge.

膨張機構5の使用下限回転数Rexp_minは、膨張機構5や膨張機構制御手段11の保護するための下限値として設定されている。ステップ160において、膨張機構5の回転数Rexpが、使用下限回転数Rexp_minより大きいと判定された場合には、
膨張機構5、および、発電機4の回転数をある一定量、低下させるように膨張機構制御手段11に指示する(ステップ170)。これにより、膨張機構5を流通する冷媒量が低下するため、吐出温度Tdや高圧側圧力を上昇させることができる。
The lower limit rotation speed Reexp_min of the expansion mechanism 5 is set as a lower limit value for protecting the expansion mechanism 5 and the expansion mechanism control means 11. If it is determined in step 160 that the rotation speed Reexp of the expansion mechanism 5 is greater than the use lower limit rotation speed Reexp_min,
The expansion mechanism control means 11 is instructed to decrease the rotation speeds of the expansion mechanism 5 and the generator 4 by a certain amount (step 170). Thereby, since the refrigerant | coolant amount which distribute | circulates the expansion mechanism 5 falls, discharge temperature Td and a high voltage | pressure side pressure can be raised.

ステップ120において、吐出温度TdがTd0+ΔT1より低いと判定され、ステップ150において、吐出温度TdがTd0−ΔT2より高いと判定された場合には、吐出温度は目標吐出温度Td0に近い、ある一定の温度範囲に入っているので、現在の膨張機構5、および、発電機4の回転数を維持するように膨張機構制御手段11に指示する(ステップ180)。   If it is determined in step 120 that the discharge temperature Td is lower than Td0 + ΔT1, and it is determined in step 150 that the discharge temperature Td is higher than Td0−ΔT2, the discharge temperature is a certain temperature close to the target discharge temperature Td0. Since it is within the range, the expansion mechanism control means 11 is instructed to maintain the current expansion mechanism 5 and the rotational speed of the generator 4 (step 180).

一方、ステップ120において、吐出温度TdがTd0+ΔT1より高いと判定され、ステップ130において、膨張機構5の回転数Rexpが、使用上限回転数Rexp_maxより大きいと判定された場合には、これ以上、膨張機構5の回転数を増加させると信頼性の低下を招く恐れがあるため、圧縮機構2、および、電動機1の回転数をある一定量、低下させるように圧縮機構制御手段10に指示する(ステップ190)。これにより、膨張機構5の使用上限回転数Rexp_maxを越えることなく、吐出温度Tdや高圧側圧力を低下させることができる。   On the other hand, if it is determined in step 120 that the discharge temperature Td is higher than Td0 + ΔT1, and it is determined in step 130 that the rotation speed Reexp of the expansion mechanism 5 is larger than the upper limit rotation speed Reexp_max, the expansion mechanism is further increased. Increasing the number of revolutions of 5 may cause a decrease in reliability. Therefore, the compression mechanism control unit 10 is instructed to reduce the number of revolutions of the compression mechanism 2 and the electric motor 1 by a certain amount (step 190). ). Thereby, the discharge temperature Td and the high-pressure side pressure can be reduced without exceeding the upper limit rotation speed Reexp_max of the expansion mechanism 5.

ステップ120において、吐出温度TdがTd0+ΔT1より低いと判定され、ステップ150において、吐出温度TdがTd0−ΔT2より低いと判定され、ステップ160において、膨張機構5の回転数Rexpが、使用下限回転数Rexp_minより小さいと判定された場合には、これ以上、膨張機構5の回転数を低下させると信頼性の低下を招く恐れがあるため、圧縮機構2、および、電動機1の回転数をある一定量、増加させるように圧縮機構制御手段10に指示する(ステップ200)。これにより、膨張機構5の使用下限回転数Rexp_minを越えることなく、吐出温度Tdや高圧側圧力を上昇させることができる。   In step 120, it is determined that the discharge temperature Td is lower than Td0 + ΔT1, and in step 150, it is determined that the discharge temperature Td is lower than Td0−ΔT2, and in step 160, the rotation speed Reexp of the expansion mechanism 5 is the lower limit rotation speed Reexp_min. If it is determined that the rotational speed of the expansion mechanism 5 is further reduced, the reliability of the compression mechanism 2 and the electric motor 1 may be reduced by a certain amount. The compression mechanism control means 10 is instructed to increase (step 200). Thereby, the discharge temperature Td and the high-pressure side pressure can be increased without exceeding the lower limit rotation speed Reexp_min of the expansion mechanism 5.

以上のステップ120から180の動作によれば、吐出温度Tdが目標吐出温度の上限値(Td0+ΔT1)を越える場合には、膨張機構5、および、発電機4の回転数を増加させるように変更し、吐出温度Tdを下げるようにするので、冷凍サイクル装置を保護するために圧縮機構2などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。また、吐出温度Tdが目標吐出温度の下限値(Td0−ΔT2)を下回る場合には、膨張機構5、および、発電機4の回転数を低下させるように変更し、吐出温度Tdを上げるようにするので、不必要に吐出温度Tdを下げることなく、安定的に冷凍サイクル装置を運転することができる。なお、以上のステップ120から180の動作によって、決定された膨張機構5の目標膨張機構回転数をこれ以降、第1目標膨張機構回転数と呼ぶ。   According to the operations from step 120 to step 180 described above, when the discharge temperature Td exceeds the upper limit value (Td0 + ΔT1) of the target discharge temperature, the rotation speed of the expansion mechanism 5 and the generator 4 is changed to be increased. Since the discharge temperature Td is lowered, it is not necessary to stop the operation of the compression mechanism 2 or the like in order to protect the refrigeration cycle apparatus, and the refrigeration cycle apparatus can be stably operated. Further, when the discharge temperature Td is lower than the lower limit value (Td0−ΔT2) of the target discharge temperature, the expansion mechanism 5 and the generator 4 are changed so as to decrease the rotation speed, and the discharge temperature Td is increased. Therefore, the refrigeration cycle apparatus can be stably operated without unnecessarily lowering the discharge temperature Td. The target expansion mechanism rotational speed of the expansion mechanism 5 determined by the operations of steps 120 to 180 is hereinafter referred to as a first target expansion mechanism rotational speed.

さらに、ステップ190から200の動作によれば、吐出温度Tdが目標吐出温度の上限値(Td0+ΔT1)を越える場合で、膨張機構5の回転数Rexpが、使用上限回転数Rexp_maxより大きい場合には、膨張機構5、および、発電機4の回転数を増加させ、吐出温度Tdを下げるかわりに、圧縮機構2、および、電動機1の回転数を減少させ、吐出温度Tdを下げるようにするので、膨張機構5などを保護するために圧縮機構2などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。   Further, according to the operations of Steps 190 to 200, when the discharge temperature Td exceeds the upper limit value (Td0 + ΔT1) of the target discharge temperature and the rotation speed Reexp of the expansion mechanism 5 is larger than the use upper limit rotation speed Reexp_max, Instead of increasing the rotation speed of the expansion mechanism 5 and the generator 4 and decreasing the discharge temperature Td, the rotation speed of the compression mechanism 2 and the electric motor 1 is decreased and the discharge temperature Td is decreased. There is no need to stop the operation of the compression mechanism 2 or the like to protect the mechanism 5 or the like, and the refrigeration cycle apparatus can be stably operated.

また、吐出温度Tdが目標吐出温度の下限値(Td0−ΔT2)を下回る場合で、膨張機構5の回転数Rexpが、使用下限回転数Rexp_minより小さい場合には、膨張機構5、および、発電機4の回転数を低下させ、吐出温度Tdを上げるかわりに、圧縮機構2、および、電動機1の回転数を増加させ、吐出温度Tdを上げるようにするので、膨
張機構5などを保護するために圧縮機構2などの運転を停止する必要が無くなり、安定的に冷凍サイクル装置を運転することができる。
When the discharge temperature Td is lower than the lower limit value (Td0−ΔT2) of the target discharge temperature and the rotation speed Reexp of the expansion mechanism 5 is smaller than the use lower limit rotation speed Reexp_min, the expansion mechanism 5 and the generator In order to protect the expansion mechanism 5 and the like, the rotation speed of the compression mechanism 2 and the electric motor 1 is increased and the discharge temperature Td is increased instead of lowering the rotation speed 4 and increasing the discharge temperature Td. There is no need to stop the operation of the compression mechanism 2 and the like, and the refrigeration cycle apparatus can be stably operated.

なお、上述のステップ190から200の動作を省略しても、ステップ120から180の動作による効果を得られることは明らかである。また、ステップ190、ステップ200のいずれか一方の動作を省略しても、省略しないステップの動作による効果が得られることは明らかである。   Obviously, even if the operations in steps 190 to 200 are omitted, the effects of the operations in steps 120 to 180 can be obtained. Further, it is clear that even if one of the operations of Step 190 and Step 200 is omitted, the effect of the operation of the step that is not omitted can be obtained.

また、ΔT1、ΔT2は同じ値としてもよいし、異なる値としてもよい。さらに、ΔT1、ΔT2のいずれか一方、あるいは、両方を0としてもよい。   ΔT1 and ΔT2 may be the same value or different values. Furthermore, one or both of ΔT1 and ΔT2 may be set to zero.

(実施の形態2)
本発明の第2の実施の形態における冷凍サイクル装置の起動時の制御方法を、図3に示すタイムチャート、図4に示す膨張機構5の制御のフローチャート、図5に示す圧縮機構2の制御のフローチャートを用いて説明する。なお、冷凍サイクル装置の概略構成は図1と同様であるため、説明を省略する。
(Embodiment 2)
The control method at the time of starting of the refrigeration cycle apparatus in the second embodiment of the present invention, the time chart shown in FIG. 3, the flowchart of the control of the expansion mechanism 5 shown in FIG. 4, the control of the compression mechanism 2 shown in FIG. This will be described with reference to a flowchart. The schematic configuration of the refrigeration cycle apparatus is the same as that shown in FIG.

利用者からの指示や、予め定められた運転時刻になると、電子制御装置15により冷凍サイクル装置の起動が行われる。本実施の形態では、圧縮機構2を起動させる前に膨張機構5を起動させる。膨張機構5、実質的には発電機4は、図4に示すフローチャートのように、膨張機構制御手段11により制御される。電子制御装置15は、外気温度検知手段13により外気温度を検知し(ステップ300)、入水温度検知手段14により入水温度を検知する(ステップ310)。検知した外気温度や入水温度などから冷凍サイクル装置の起動時における膨張機構5の回転数である第2目標膨張機構回転数を算出する(ステップ320)。この第2目標膨張機構回転数は、起動時において圧縮機構2や膨張機構5などの構成要素の使用温度上限や圧力上限を越えないように、外気温度が高いほど回転数が高く、入水温度が高いほど回転数が高くなるように、かつ、第1の実施の形態で説明した第1目標膨張機構回転数より小さい値が設定されている。   When an instruction from the user or a predetermined operation time is reached, the electronic control device 15 activates the refrigeration cycle device. In the present embodiment, the expansion mechanism 5 is activated before the compression mechanism 2 is activated. The expansion mechanism 5, substantially the generator 4, is controlled by the expansion mechanism control means 11, as shown in the flowchart of FIG. The electronic control unit 15 detects the outside air temperature by the outside air temperature detecting means 13 (Step 300), and detects the incoming water temperature by the incoming water temperature detecting means 14 (Step 310). A second target expansion mechanism rotational speed that is the rotational speed of the expansion mechanism 5 at the time of starting the refrigeration cycle apparatus is calculated from the detected outside air temperature, incoming water temperature, and the like (step 320). The second target expansion mechanism rotational speed is such that the higher the outside air temperature is, the higher the rotational speed is and the incoming water temperature is such that the operating temperature upper limit and pressure upper limit of the components such as the compression mechanism 2 and the expansion mechanism 5 are not exceeded at startup. A value smaller than the first target expansion mechanism rotation speed described in the first embodiment is set so that the higher the rotation speed, the higher the rotation speed.

次に、第2目標膨張機構回転数で膨張機構5を運転(起動)する(ステップ330)。さらに、膨張機構5の起動後、所定時間Te1経過したかを判定する(ステップ340)。所定時間Te1経過していない場合には、ステップ330に戻り、第2目標膨張機構回転数での運転を継続する。一方、所定時間Te1経過した場合には、第1の実施の形態で説明した図2のフローチャートのステップ100〜200へと進み、第1目標膨張機構回転数で運転する。   Next, the expansion mechanism 5 is operated (activated) at the second target expansion mechanism rotation speed (step 330). Further, it is determined whether a predetermined time Te1 has elapsed after the expansion mechanism 5 is activated (step 340). If the predetermined time Te1 has not elapsed, the process returns to step 330, and the operation at the second target expansion mechanism rotational speed is continued. On the other hand, when the predetermined time Te1 has elapsed, the process proceeds to steps 100 to 200 in the flowchart of FIG. 2 described in the first embodiment, and the operation is performed at the first target expansion mechanism rotational speed.

一方、圧縮機構2、実質的には駆動源である電動機1は、図5に示すフローチャートのように、圧縮機構制御手段10により制御される。電子制御装置15は、外気温度検知手段13により外気温度を検知し(ステップ400)、入水温度検知手段14により入水温度を検知する(ステップ410)。検知した外気温度や入水温度などから冷凍サイクル装置の起動時における圧縮機構2の回転数である第2目標圧縮機構回転数を算出する(ステップ420)。この第2目標圧縮機構回転数は、起動時において圧縮機構2や膨張機構5などの構成要素の使用温度上限や圧力上限を越えないように、かつ、第1の実施の形態で説明した第1目標圧縮機構回転数より小さい値が設定されている。   On the other hand, the compression mechanism 2, substantially the electric motor 1 as a drive source, is controlled by the compression mechanism control means 10 as shown in the flowchart of FIG. The electronic control unit 15 detects the outside air temperature by the outside air temperature detecting means 13 (step 400), and detects the incoming water temperature by the incoming water temperature detecting means 14 (step 410). A second target compression mechanism rotational speed that is the rotational speed of the compression mechanism 2 at the time of starting the refrigeration cycle apparatus is calculated from the detected outside air temperature, incoming water temperature, and the like (step 420). The second target compression mechanism rotational speed does not exceed the upper use temperature limit and the upper pressure limit of components such as the compression mechanism 2 and the expansion mechanism 5 at the time of start-up, and is the first described in the first embodiment. A value smaller than the target compression mechanism rotational speed is set.

これにより、起動時に圧縮機構2を停止状態から急激に回転数を増加させた場合に生じる恐れのある潤滑油が不足するなどの信頼性低下を防止できる。次に、膨張機構5が起動してから、所定時間T0経過したかを判定する(ステップ430)。所定時間T0経過していない場合には、ステップ400に戻り、外気温度、入水温度の検知を更新し、第2目標圧縮機構回転数の算出を更新する。所定時間T0経過した場合には、第2目標圧縮機構
回転数で圧縮機構2を運転(起動)する(ステップ440)。
Thereby, it is possible to prevent a decrease in reliability such as lack of lubricating oil that may occur when the rotation speed of the compression mechanism 2 is suddenly increased from a stopped state at the time of startup. Next, it is determined whether a predetermined time T0 has elapsed since the expansion mechanism 5 was activated (step 430). If the predetermined time T0 has not elapsed, the process returns to step 400, the detection of the outside air temperature and the incoming water temperature is updated, and the calculation of the second target compression mechanism rotation speed is updated. When the predetermined time T0 has elapsed, the compression mechanism 2 is operated (activated) at the second target compression mechanism rotation speed (step 440).

次に、圧縮機構2の起動後、所定時間Tc1経過したかを判定する(ステップ450)。所定時間Tc1経過していない場合には、ステップ440に戻り、第2目標圧縮機構回転数での運転を継続する。一方、所定時間Tc1経過した場合には、再び外気温度検知手段13により外気温度を検知し(ステップ460)、入水温度検知手段14により入水温度を検知する(ステップ470)。検知した外気温度や入水温度などから冷凍サイクル装置の安定時における圧縮機構2の回転数である第1目標圧縮機構回転数を算出する(ステップ480)。   Next, it is determined whether a predetermined time Tc1 has elapsed after the compression mechanism 2 is activated (step 450). If the predetermined time Tc1 has not elapsed, the process returns to step 440, and the operation at the second target compression mechanism rotational speed is continued. On the other hand, when the predetermined time Tc1 has elapsed, the outside air temperature detecting means 13 detects the outside air temperature again (step 460), and the incoming water temperature detecting means 14 detects the incoming water temperature (step 470). A first target compression mechanism rotational speed, which is the rotational speed of the compression mechanism 2 when the refrigeration cycle apparatus is stable, is calculated from the detected outside air temperature, incoming water temperature, and the like (step 480).

この第1目標圧縮機構回転数は、冷凍サイクルが比較的安定した場合に、必要な加熱量が確保できるように設定されている。また、所定時間Tc1は(所定時間Te1−所定時間T0)より大きい値が設定されている。次に、圧縮機構2の回転数を第1目標圧縮機構回転数に変更し運転する(ステップ490)。その後、ステップ460に戻り、外気温度、入水温度の検知の更新、第1目標圧縮機構回転数の算出の更新を、定められた制御周期で繰り返し、他の指示、例えば、冷凍サイクル装置の停止指示まで、第1目標圧縮機構回転数での運転を継続する。   The first target compression mechanism rotational speed is set so that a necessary heating amount can be secured when the refrigeration cycle is relatively stable. The predetermined time Tc1 is set to a value greater than (predetermined time Te1-predetermined time T0). Next, the rotation speed of the compression mechanism 2 is changed to the first target compression mechanism rotation speed (step 490). Thereafter, the process returns to step 460, and the update of the detection of the outside air temperature and the incoming water temperature and the update of the calculation of the first target compression mechanism rotation speed are repeated at a predetermined control cycle, and another instruction, for example, a stop instruction of the refrigeration cycle apparatus Until then, the operation at the first target compression mechanism rotational speed is continued.

以上の動作によれば、図2に示すタイムチャートのように、膨張機構5が外気温度、入水温度から算出された第2目標膨張機構回転数で起動した後、所定時間T0経過後、圧縮機構2が外気温度、入水温度から算出された第2目標圧縮機構回転数で起動する。このため、圧縮機構2の起動の際に、膨張機構5が停止しているために急激に高圧側圧力が上昇するなどの不具合が生じることなく、安定した冷凍サイクル装置の起動が実現できる。また、第2目標膨張機構回転数は外気温度、入水温度に応じて、高圧側圧力が上昇しやすい状態ほど、回転数が大きくなるように設定されているので、さらに、急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   According to the above operation, as shown in the time chart of FIG. 2, after the expansion mechanism 5 is started at the second target expansion mechanism rotational speed calculated from the outside air temperature and the incoming water temperature, after the predetermined time T0 has elapsed, the compression mechanism 2 starts at the second target compression mechanism rotation speed calculated from the outside air temperature and the incoming water temperature. For this reason, when the compression mechanism 2 is started, a stable start of the refrigeration cycle apparatus can be realized without causing problems such as a rapid increase in the high-pressure side pressure because the expansion mechanism 5 is stopped. The second target expansion mechanism rotation speed is set so that the higher the high pressure side pressure is, the higher the rotation speed is, depending on the outside air temperature and the incoming water temperature. The rise can be prevented, and a stable refrigeration cycle apparatus can be started.

また、圧縮機構2の起動後、所定時間Tc1経過すると、圧縮機構2の回転数は、外気温度、入水温度から算出された第1目標圧縮機構回転数に増加するが、膨張機構5の起動後、所定時間Te1経過した時点で、膨張機構5の回転数は、第1の実施の形態で説明した第1目標膨張機構回転数へと予め増加する。このように、圧縮機構2の回転数が増加するより前に、膨張機構5の回転数が予め大きくなるように設定しているため、圧縮機構2の回転数が増加する際の急激な高圧側圧力の上昇を防止でき、安定した冷凍サイクル装置の起動が実現できる。   When the predetermined time Tc1 elapses after the compression mechanism 2 is activated, the rotation speed of the compression mechanism 2 increases to the first target compression mechanism rotation speed calculated from the outside air temperature and the incoming water temperature. When the predetermined time Te1 has elapsed, the rotational speed of the expansion mechanism 5 is increased in advance to the first target expansion mechanism rotational speed described in the first embodiment. As described above, since the rotation speed of the expansion mechanism 5 is set to be increased in advance before the rotation speed of the compression mechanism 2 is increased, the rapid high pressure side when the rotation speed of the compression mechanism 2 is increased is set. An increase in pressure can be prevented, and a stable refrigeration cycle apparatus can be started.

なお、本実施の形態では、圧縮機構2の回転数を増加させる前に、膨張機構5の回転数を増加させるものとして説明したが、圧縮機構2の回転数を増加させると同時に、膨張機構5の回転数を増加させる(すなわち、T0を0とする)場合でも同様の効果が得られる。   In the present embodiment, it has been described that the rotation speed of the expansion mechanism 5 is increased before the rotation speed of the compression mechanism 2 is increased. However, at the same time as the rotation speed of the compression mechanism 2 is increased, the expansion mechanism 5 is increased. The same effect can be obtained even when the number of rotations is increased (that is, T0 is set to 0).

また、本実施の形態では、第1目標膨張機構回転数、第2目標膨張機構回転数などは、外気温度と入水温度とに応じて決定するものとしているが、いずれか一方の温度に応じて決定するものとしてもよい。   Further, in the present embodiment, the first target expansion mechanism rotation speed, the second target expansion mechanism rotation speed, and the like are determined according to the outside air temperature and the incoming water temperature, but according to any one of the temperatures. It may be determined.

また、本実施の形態では、冷凍サイクルの変化が小さい場合での圧縮機構2の目標回転数である第1目標圧縮機構回転数、および、膨張機構5の目標回転数である第1目標膨張機構回転数に到達する以前に、それらより小さい回転数に設定された第2目標圧縮機構回転数、および、第2目標圧縮機構回転数を設けているが、第1目標圧縮機構回転数、および、第1目標膨張機構回転数に到達する以前の区間を、複数の区間に分けて、段階的に目標圧縮機構回転数、および、目標膨張機回転数を変化させるように、複数の第2目標圧縮
機構回転数、および、第2目標膨張機構回転数を設けてもよい
(実施の形態3)
本発明の第3の実施の形態における冷凍サイクル装置の起動時の制御方法を、図6に示すタイムチャート、図7に示す膨張機構5の制御のフローチャートを用いて説明する。なお、冷凍サイクル装置の概略構成は図1と同様であるため、説明を省略する。また、圧縮機構2の制御方法は第2の実施の形態と同様であるため、説明を省略する。
In the present embodiment, the first target compression mechanism rotation speed that is the target rotation speed of the compression mechanism 2 and the first target expansion mechanism that is the target rotation speed of the expansion mechanism 5 when the change in the refrigeration cycle is small. Before reaching the rotational speed, the second target compression mechanism rotational speed and the second target compression mechanism rotational speed set to a rotational speed smaller than those are provided, the first target compression mechanism rotational speed, and A plurality of second target compressions are performed so that the section before reaching the first target expansion mechanism rotational speed is divided into a plurality of sections and the target compression mechanism rotational speed and the target expander rotational speed are changed stepwise. A mechanism rotational speed and a second target expansion mechanism rotational speed may be provided (Embodiment 3).
A control method at the start of the refrigeration cycle apparatus according to the third embodiment of the present invention will be described with reference to a time chart shown in FIG. 6 and a flowchart of control of the expansion mechanism 5 shown in FIG. The schematic configuration of the refrigeration cycle apparatus is the same as that shown in FIG. Moreover, since the control method of the compression mechanism 2 is the same as that of 2nd Embodiment, description is abbreviate | omitted.

利用者からの指示や、予め定められた運転時刻になると、電子制御装置15により冷凍サイクル装置の起動が行われる。本実施の形態では、圧縮機構2を起動させる前に膨張機構5を起動させる。膨張機構5、実質的には発電機4は、図7に示すフローチャートのように、膨張機構制御手段11により制御される。電子制御装置15は、外気温度検知手段13により外気温度を検知し(ステップ500)、入水温度検知手段14により入水温度を検知する(ステップ510)。検知した外気温度や入水温度などから冷凍サイクル装置の起動時における膨張機構5の回転数である第2目標膨張機構回転数を算出する(ステップ520)。この第2目標膨張機構回転数は、起動時において圧縮機構2や膨張機構5などの構成要素の使用温度上限や圧力上限を越えないように、外気温度が高いほど回転数が高く、入水温度が高いほど回転数が高くなるように、かつ、第1の実施の形態で説明した第1目標膨張機構回転数より小さい値が設定されている。   When an instruction from the user or a predetermined operation time is reached, the electronic control device 15 activates the refrigeration cycle device. In the present embodiment, the expansion mechanism 5 is activated before the compression mechanism 2 is activated. The expansion mechanism 5, substantially the generator 4, is controlled by the expansion mechanism control means 11, as shown in the flowchart of FIG. The electronic control unit 15 detects the outside air temperature by the outside air temperature detecting means 13 (step 500), and detects the incoming water temperature by the incoming water temperature detecting means 14 (step 510). A second target expansion mechanism rotational speed that is the rotational speed of the expansion mechanism 5 at the time of starting the refrigeration cycle apparatus is calculated from the detected outside air temperature, incoming water temperature, and the like (step 520). The second target expansion mechanism rotational speed is such that the higher the outside air temperature is, the higher the rotational speed is and the incoming water temperature is such that the operating temperature upper limit and pressure upper limit of the components such as the compression mechanism 2 and the expansion mechanism 5 are not exceeded at startup. A value smaller than the first target expansion mechanism rotation speed described in the first embodiment is set so that the higher the rotation speed, the higher the rotation speed.

次に、第2目標膨張機構回転数で膨張機構5を運転(起動)する(ステップ530)。さらに、膨張機構5の起動後、所定時間Te2経過したかを判定する(ステップ540)。所定時間Te2経過していない場合には、ステップ530に戻り、第2目標膨張機構回転数での運転を継続する。一方、所定時間Te2経過した場合には、外気温度検知手段13により外気温度の検知を更新し(ステップ550)、入水温度検知手段14により入水温度の検知を更新する(ステップ560)。   Next, the expansion mechanism 5 is operated (activated) at the second target expansion mechanism rotation speed (step 530). Further, it is determined whether a predetermined time Te2 has elapsed after the expansion mechanism 5 is started (step 540). If the predetermined time Te2 has not elapsed, the process returns to step 530, and the operation at the second target expansion mechanism rotational speed is continued. On the other hand, when the predetermined time Te2 has elapsed, the detection of the outside air temperature is updated by the outside air temperature detecting means 13 (step 550), and the detection of the incoming water temperature is updated by the incoming water temperature detecting means 14 (step 560).

検知した外気温度や入水温度などから冷凍サイクル装置の起動時における膨張機構5の回転数である第3目標膨張機構回転数を算出する(ステップ570)。この第3目標膨張機構回転数は、起動時において圧縮機構2や膨張機構5などの構成要素の使用温度上限や圧力上限を越えないように、外気温度が高いほど回転数が高く、入水温度が高いほど回転数が高くなるように、かつ、第1の実施の形態で説明した第1目標膨張機構回転数より大きい値に設定されている。   A third target expansion mechanism rotational speed that is the rotational speed of the expansion mechanism 5 at the time of starting the refrigeration cycle apparatus is calculated from the detected outside air temperature, incoming water temperature, and the like (step 570). The third target expansion mechanism rotational speed is such that the higher the outside air temperature is, the higher the rotational speed is, and the incoming water temperature is such that the operating temperature upper limit and pressure upper limit of the components such as the compression mechanism 2 and the expansion mechanism 5 are not exceeded at startup. It is set to a value larger than the first target expansion mechanism rotation speed described in the first embodiment so that the higher the rotation speed, the higher the rotation speed.

次に、第3目標膨張機構回転数で膨張機構5を運転する(ステップ580)。さらに、膨張機構5の起動後、所定時間Te3経過したかを判定する(ステップ590)。所定時間Te3経過していない場合には、ステップ550に戻り、再び、外気温度や入水温度の検知の更新と第3目標膨張機構回転数の演算を行った後、第3目標膨張機構回転数での運転を継続する。一方、所定時間Te3経過した場合には、第1の実施の形態で説明した図2のフローチャートのステップ100〜200へと進み、第1目標膨張機構回転数で運転する。   Next, the expansion mechanism 5 is operated at the third target expansion mechanism rotation speed (step 580). Further, it is determined whether a predetermined time Te3 has elapsed after the expansion mechanism 5 is activated (step 590). If the predetermined time Te3 has not elapsed, the process returns to step 550, and after updating the detection of the outside air temperature and the incoming water temperature and calculating the third target expansion mechanism rotational speed again, the third target expansion mechanism rotational speed is reached. Continue driving. On the other hand, when the predetermined time Te3 has elapsed, the process proceeds to steps 100 to 200 in the flowchart of FIG. 2 described in the first embodiment, and the operation is performed at the first target expansion mechanism rotational speed.

以上の動作によれば、図6に示すタイムチャートのように、膨張機構5が外気温度、入水温度から算出された第2目標膨張機構回転数で起動した後、所定時間Te3経過すると、膨張機構5の回転数は、第1の実施の形態で説明した第1目標膨張機構回転数へと増加する。しかし、所定時間Te3経過する以前の所定時間Te2経過した時点で、膨張機構5の回転数は、第2目標膨張機構回転数より大きい値に設定された第3目標膨張機構回転数で運転されるので、膨張機構5の回転数が、第2目標膨張機構回転数から第1目標膨張機構回転数へと増加する際の急激な高圧側圧力の変化を防止でき、起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   According to the above operation, as shown in the time chart of FIG. 6, when the expansion mechanism 5 is started at the second target expansion mechanism rotation speed calculated from the outside air temperature and the incoming water temperature, when the predetermined time Te3 has elapsed, the expansion mechanism 5 The rotational speed of 5 increases to the first target expansion mechanism rotational speed described in the first embodiment. However, when the predetermined time Te2 elapses before the predetermined time Te3 elapses, the rotation speed of the expansion mechanism 5 is operated at the third target expansion mechanism rotation speed set to a value larger than the second target expansion mechanism rotation speed. Therefore, it is possible to prevent a rapid change in the high-pressure side pressure when the rotation speed of the expansion mechanism 5 increases from the second target expansion mechanism rotation speed to the first target expansion mechanism rotation speed, and to stabilize the startup time. Activation of the refrigeration cycle apparatus can be realized.

また、本実施の形態では、第3目標膨張機構回転数は、外気温度と入水温度とに応じて決定するものとしているが、いずれか一方の温度に応じて決定するものとしてもよい。   In the present embodiment, the third target expansion mechanism rotational speed is determined according to the outside air temperature and the incoming water temperature, but may be determined according to any one of the temperatures.

(実施の形態4)
本発明の第4の実施の形態における冷凍サイクル装置の起動時の制御方法を、図8に示す膨張機構5の制御のフローチャートを用いて説明する。図8において、図7と同じ制御ステップについては、同一の番号を付し、説明を省略する。また、冷凍サイクル装置の概略構成は図1と同様であるため、説明を省略する。さらに、圧縮機構2の制御方法は第2の実施の形態と同様であるため、説明を省略する。
(Embodiment 4)
A control method at the start of the refrigeration cycle apparatus according to the fourth embodiment of the present invention will be described with reference to a control flowchart of the expansion mechanism 5 shown in FIG. 8, the same control steps as those in FIG. 7 are denoted by the same reference numerals, and description thereof is omitted. The schematic configuration of the refrigeration cycle apparatus is the same as that shown in FIG. Furthermore, since the control method of the compression mechanism 2 is the same as that of the second embodiment, description thereof is omitted.

ステップ580において第3目標膨張機構回転数で膨張機構5を運転し、さらに、膨張機構5の起動後、所定時間Te3経過したかを判定する(ステップ590)。所定時間Te3経過していない場合には、吐出温度検知手段12により吐出温度Tdを検知する(ステップ600)。目標吐出温度Td0と検知した吐出温度Tdの差がある一定値ΔT3より小さいか否かを判定する(ステップ610)。なお、第1の実施の形態と同様に、目標吐出温度Td0は、外気温度や入水温度、利用者等が設定した目標沸上温度(給湯タンクに貯めるお湯の温度、または、放熱器6の流体出口側温度の目標値)などから、冷凍サイクルの状態が最適となるように設定されており、ΔT3は、吐出温度Tdが目標吐出温度Td0に近づいたことを判定するための微少値である。   In step 580, the expansion mechanism 5 is operated at the third target expansion mechanism rotation speed, and it is further determined whether a predetermined time Te3 has elapsed after the expansion mechanism 5 is started (step 590). If the predetermined time Te3 has not elapsed, the discharge temperature detecting means 12 detects the discharge temperature Td (step 600). It is determined whether or not the difference between the target discharge temperature Td0 and the detected discharge temperature Td is smaller than a certain value ΔT3 (step 610). As in the first embodiment, the target discharge temperature Td0 is the outside air temperature, the incoming water temperature, the target boiling temperature set by the user (the temperature of hot water stored in the hot water tank, or the fluid of the radiator 6). From the target value of the outlet side temperature), the refrigeration cycle state is set to be optimal, and ΔT3 is a minute value for determining that the discharge temperature Td has approached the target discharge temperature Td0.

ステップ610において、目標吐出温度Td0と検知した吐出温度Tdの差がある一定値ΔT3より大きいと判定された場合には、吐出温度Tdは目標吐出温度Td0に十分に近づいていないので、ステップ550に戻り、再び、外気温度や入水温度の検知の更新と第3目標膨張機構回転数の演算を行った後、第3目標膨張機構回転数での運転を継続する。一方、目標吐出温度Td0と検知した吐出温度Tdの差がある一定値ΔT3より小さいと判定された場合には、吐出温度Tdは目標吐出温度Td0に十分に近づいているので、第1の実施の形態で説明した図2のフローチャートのステップ100〜200へと進み、吐出温度を目標吐出温度に近づけるような膨張機構5の回転数である第1目標膨張機構回転数で運転する。   If it is determined in step 610 that the difference between the target discharge temperature Td0 and the detected discharge temperature Td is greater than a certain value ΔT3, the discharge temperature Td is not sufficiently close to the target discharge temperature Td0, so Returning again, after updating the detection of the outside air temperature and the incoming water temperature and calculating the third target expansion mechanism rotation speed, the operation at the third target expansion mechanism rotation speed is continued. On the other hand, when it is determined that the difference between the target discharge temperature Td0 and the detected discharge temperature Td is smaller than a certain value ΔT3, the discharge temperature Td is sufficiently close to the target discharge temperature Td0. The process proceeds to steps 100 to 200 in the flowchart of FIG. 2 described in the embodiment, and the operation is performed at the first target expansion mechanism rotation speed that is the rotation speed of the expansion mechanism 5 that brings the discharge temperature close to the target discharge temperature.

また、ステップ590において、所定時間Te3経過したと判定された場合にも、第1の実施の形態で説明した図2のフローチャートのステップ100〜200へと進み、第1目標膨張機構回転数で運転する。   If it is determined in step 590 that the predetermined time Te3 has elapsed, the process proceeds to steps 100 to 200 in the flowchart of FIG. 2 described in the first embodiment, and the operation is performed at the first target expansion mechanism rotational speed. To do.

以上の動作によれば、所定時間Te3を経過していなくても、吐出温度Tdが目標吐出温度Td0に近づいた場合には、所定時間Te3を経過した場合と同様に、次の目標膨張機構回転数に移行するものである。すなわち、吐出温度Tdが目標吐出温度Td0に近づいた場合には、所定時間Te3を経過したものとみなすものである。   According to the above operation, even if the predetermined time Te3 has not elapsed, when the discharge temperature Td approaches the target discharge temperature Td0, the next target expansion mechanism rotation is performed as in the case where the predetermined time Te3 has elapsed. The number will shift. That is, when the discharge temperature Td approaches the target discharge temperature Td0, it is considered that the predetermined time Te3 has elapsed.

このような動作によれば、所定時間Te3経過する以前であっても、吐出温度Tdが目標吐出温度Td0に近づいた場合には、膨張機構5の回転数は、第1目標膨張機構回転数に移行するので、不必要に第3目標膨張機構回転数で運転を行う時間を短縮でき、さらに起動時間を短縮しつつ安定した冷凍サイクル装置の起動が実現できる。   According to such an operation, even before the predetermined time Te3 has elapsed, when the discharge temperature Td approaches the target discharge temperature Td0, the rotation speed of the expansion mechanism 5 becomes the first target expansion mechanism rotation speed. Since the shift is made, it is possible to unnecessarily reduce the time for operation at the third target expansion mechanism rotation speed, and to realize stable start-up of the refrigeration cycle apparatus while reducing the start-up time.

なお、本実施の形態では、吐出温度Tdが目標吐出温度Td0に近づいた場合には、所定時間Te3を経過したものとみなすものとしたが、利用側熱交換器である放熱器3から流出する利用側流体出口温度(すなわち、沸上温度)が、予め定められた利用側流体出口温度の目標温度(すなわち、目標沸上温度)に近づけば、所定時間Te3を経過したものとみなすものとしてもよい。あるいは、吐出温度Tdが予め定められた目標沸上温度よりある一定温度差以上高くなれば、所定時間Te3を経過したものとみなすものとしてもよ
い。また、ΔT3は0としてもよい。
In the present embodiment, when the discharge temperature Td approaches the target discharge temperature Td0, it is assumed that the predetermined time Te3 has elapsed, but it flows out of the radiator 3 that is the use side heat exchanger. If the use side fluid outlet temperature (that is, boiling temperature) approaches the target temperature (that is, target boiling temperature) of the predetermined use side fluid outlet temperature, it may be considered that the predetermined time Te3 has elapsed. Good. Alternatively, if the discharge temperature Td is higher than a predetermined target boiling temperature by a certain temperature difference or more, it may be considered that the predetermined time Te3 has elapsed. ΔT3 may be 0.

さらに、第2から第3の実施の形態における所定時間Te1、Te2、Tc1などにおいても、吐出温度Tdが目標吐出温度Td0に近づいた場合や、沸上温度が目標沸上温度に近づいた場合や、吐出温度Tdが目標沸上温度よりある一定温度差以上高くなった場合にも、それぞれの所定時間を経過したとみなすようにしてもよい。   Further, also in the predetermined times Te1, Te2, Tc1, etc. in the second to third embodiments, when the discharge temperature Td approaches the target discharge temperature Td0, or when the boiling temperature approaches the target boiling temperature, Even when the discharge temperature Td becomes higher than the target boiling temperature by a certain temperature difference or more, it may be considered that each predetermined time has passed.

また、冷媒がCO冷媒の場合には、高圧側圧力は凝縮温度に依存しない超臨界状態での圧力となるために、高圧側圧力が上昇しやすいが、以上の本実施の形態によれば、機器を保護するために圧縮機構の運転を停止することなく、安定した冷凍サイクル装置の運転が実現できる。 When the refrigerant is a CO 2 refrigerant, the high-pressure side pressure is a pressure in a supercritical state that does not depend on the condensation temperature, and thus the high-pressure side pressure tends to increase. According to the above embodiment, Therefore, stable operation of the refrigeration cycle apparatus can be realized without stopping the operation of the compression mechanism to protect the equipment.

本発明の冷凍サイクル装置の制御方法およびそれを用いた冷凍サイクル装置は、膨張機構を備えた冷凍サイクル装置において、適切に膨張機構の回転数を制御し、冷凍サイクル装置を安定して運転させることが可能となるため、膨張機構を備えた給湯機、空気調和機などの用途に適用できる。   A control method for a refrigeration cycle apparatus according to the present invention and a refrigeration cycle apparatus using the same, in a refrigeration cycle apparatus provided with an expansion mechanism, appropriately control the number of rotations of the expansion mechanism and stably operate the refrigeration cycle apparatus. Therefore, it can be applied to uses such as a water heater and an air conditioner equipped with an expansion mechanism.

本発明の実施の形態1〜4における冷凍サイクル装置を示す構成図The block diagram which shows the refrigerating-cycle apparatus in Embodiment 1-4 of this invention. 本発明の実施の形態1における膨張機構の制御のフローチャートFlowchart of control of expansion mechanism in Embodiment 1 of the present invention 本発明の実施の形態2における制御のタイムチャートTime chart of control in Embodiment 2 of the present invention 本発明の実施の形態2における膨張機構の制御のフローチャートFlowchart of control of expansion mechanism in embodiment 2 of the present invention 本発明の実施の形態2における圧縮機構の制御のフローチャートFlowchart of control of compression mechanism in Embodiment 2 of the present invention 本発明の実施の形態3における制御のタイムチャートTime chart of control in Embodiment 3 of the present invention 本発明の実施の形態3における膨張機構の制御のフローチャートFlowchart of control of expansion mechanism in Embodiment 3 of the present invention 本発明の実施の形態4における膨張機構の制御のフローチャートFlowchart of control of expansion mechanism in embodiment 4 of the present invention

符号の説明Explanation of symbols

1 電動機
2 圧縮機構
3 利用側熱交換器(放熱器)
4 発電機
5 膨張機構
6 熱源側熱交換器(蒸発器)
7 利用流体搬送手段(給水ポンプ)
8 給湯タンク
9 熱源流体搬送手段(送風装置)
10 圧縮機構制御手段
11 膨張機構制御手段
12 吐出温度検知手段
13 外気温度検知手段
14 入水温度検知手段
15 電子制御手段15
A 冷媒回路
B 流体回路
DESCRIPTION OF SYMBOLS 1 Electric motor 2 Compression mechanism 3 Use side heat exchanger (heat radiator)
4 Generator 5 Expansion mechanism 6 Heat source side heat exchanger (evaporator)
7 Fluid transport means (water supply pump)
8 Hot water tank 9 Heat source fluid transfer means (blower)
DESCRIPTION OF SYMBOLS 10 Compression mechanism control means 11 Expansion mechanism control means 12 Discharge temperature detection means 13 Outside air temperature detection means 14 Incoming water temperature detection means 15 Electronic control means 15
A Refrigerant circuit B Fluid circuit

Claims (13)

少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、少なくとも前記圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、前記膨張機構の回転数を制御することを特徴とする冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism that performs power recovery, and a use side heat exchanger, at least a first target expansion mechanism rotational speed determined from a discharge temperature of the compression mechanism And controlling the number of rotations of the expansion mechanism. 前記圧縮機構の吐出温度が、予め定められた目標吐出温度より高い場合には、前記膨張機構の回転数を増加させ、前記目標吐出温度より低い場合には、前記膨張機構の回転数を低下させることを特徴とする請求項1に記載の冷凍サイクル装置の制御方法。 When the discharge temperature of the compression mechanism is higher than a predetermined target discharge temperature, the rotation speed of the expansion mechanism is increased. When the discharge temperature of the compression mechanism is lower than the target discharge temperature, the rotation speed of the expansion mechanism is decreased. The control method of the refrigerating-cycle apparatus of Claim 1 characterized by the above-mentioned. 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、前記圧縮機構の吐出温度が、予め定められた目標吐出温度より高い場合であって、前記膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の上限値を超える場合には、前記圧縮機構の回転数を低下させることを特徴とする冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, the discharge temperature of the compression mechanism is higher than a predetermined target discharge temperature. When the rotation speed of the expansion mechanism exceeds a predetermined upper limit value of the use range of the rotation speed of the expansion mechanism, the rotation speed of the compression mechanism is reduced. . 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、前記圧縮機構の吐出温度が、予め定められた目標吐出温度より低い場合であって、前記膨張機構の回転数が予め定められた膨張機構の回転数の使用範囲の下限値を超える場合には、前記圧縮機構の回転数を増加させることを特徴とする冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, the discharge temperature of the compression mechanism is lower than a predetermined target discharge temperature. When the rotation speed of the expansion mechanism exceeds a predetermined lower limit value of the use range of the rotation speed of the expansion mechanism, the rotation speed of the compression mechanism is increased. . 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、前記圧縮機構の回転数を変更すると同時、あるいは、変更する前に、前記膨張機構の回転数を変更することを特徴とするの冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, the expansion is performed at the same time as or before the rotation speed of the compression mechanism is changed. A control method for a refrigeration cycle apparatus, wherein the number of rotations of the mechanism is changed. 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置の起動時の制御方法であって、前記熱源側熱交換器に流入する熱源側流体温度と前記利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、前記膨張機構の回転数を所定時間、維持することを特徴とする冷凍サイクル装置の制御方法。 At least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a control method at the time of start-up of a refrigeration cycle apparatus including a use side heat exchanger, the heat source side fluid flowing into the heat source side heat exchanger A refrigeration characterized in that the rotation speed of the expansion mechanism is maintained for a predetermined time at a second target expansion mechanism rotation speed determined from at least one of a temperature and a utilization side fluid temperature flowing into the utilization side heat exchanger. Control method for cycle equipment. 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、前記熱源側熱交換器に流入する熱源側流体温度と前記利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、前記膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、少なくとも前記圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、前記膨張機構の回転数を制御することを特徴とする冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, the heat source side fluid temperature flowing into the heat source side heat exchanger and the use side heat exchanger The rotation speed of the expansion mechanism is maintained for a predetermined time to the second target expansion mechanism rotation speed determined from at least one of the use-side fluid temperatures flowing into the gas, and after a predetermined time has passed, at least the discharge temperature of the compression mechanism A control method for a refrigeration cycle apparatus, wherein the rotation speed of the expansion mechanism is controlled so as to be a first target expansion mechanism rotation speed determined from 少なくとも圧縮機構、熱源側熱交換器、動力回収を行う膨張機構、利用側熱交換器を備えた冷凍サイクル装置において、前記熱源側熱交換器に流入する熱源側流体温度と前記利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第2目標膨張機構回転数に、前記膨張機構の回転数を所定時間、維持し、さらに所定時間経過後、前記熱源側熱交換器に流入する熱源側流体温度と前記利用側熱交換器に流入する利用側流体温度の少なくとも一方の温度から決定する第3目標膨張機構回転数に、前記膨張機構の回転数を制御し、さらに所定経過後、少なくとも前記圧縮機構の吐出温度から決定する第1目標膨張機構回転数となるように、前記膨張機構の回転数を制御することを特徴とする冷凍サイクル装置の制御方法。 In a refrigeration cycle apparatus including at least a compression mechanism, a heat source side heat exchanger, an expansion mechanism for recovering power, and a use side heat exchanger, the heat source side fluid temperature flowing into the heat source side heat exchanger and the use side heat exchanger The rotation speed of the expansion mechanism is maintained for a predetermined time to the second target expansion mechanism rotation speed determined from at least one of the use side fluid temperatures flowing into the heat source, and after the predetermined time has passed, the heat source side heat exchanger The rotation speed of the expansion mechanism is controlled to a third target expansion mechanism rotation speed determined from at least one of the flowing heat source side fluid temperature and the utilization side fluid temperature flowing into the utilization side heat exchanger. Thereafter, the rotation speed of the expansion mechanism is controlled so as to be at least a first target expansion mechanism rotation speed determined from the discharge temperature of the compression mechanism. 前記圧縮機構の吐出温度が予め定められた目標吐出温度に近づけば、前記所定時間を終了したと判定することを特徴とする請求項6〜8のいずれか1項に記載の冷凍サイクル装置の制御方法。 The control of the refrigeration cycle apparatus according to any one of claims 6 to 8, wherein when the discharge temperature of the compression mechanism approaches a predetermined target discharge temperature, it is determined that the predetermined time has ended. Method. 前記利用側熱交換器に流入する利用側流体温度が予め定められた目標温度に近づけば、前記所定時間を終了したと判定することを特徴とする請求項6〜8のいずれか1項に記載の冷凍サイクル装置の制御方法。 9. The apparatus according to claim 6, wherein the predetermined time is determined to have ended when a use side fluid temperature flowing into the use side heat exchanger approaches a predetermined target temperature. Method for controlling the refrigeration cycle apparatus. 前記圧縮機構の吐出温度が予め定められた前記利用側熱交換器に流入する利用側流体温度の目標温度よりある一定温度差以上高くなれば、前記所定時間を終了したと判定することを特徴とする請求項6〜8のいずれか1項に記載の冷凍サイクル装置の制御方法。 If the discharge temperature of the compression mechanism is higher than a predetermined target temperature of the use side fluid temperature flowing into the use side heat exchanger, the predetermined time is determined to have ended. The control method of the refrigerating-cycle apparatus of any one of Claims 6-8 to do. 請求項1〜11のいずれか1項に記載の制御方法を用いることを特徴とする冷凍サイクル装置。 A refrigeration cycle apparatus using the control method according to any one of claims 1 to 11. 冷媒が二酸化炭素であることを特徴とする請求項12に記載の冷凍サイクル装置。 The refrigeration cycle apparatus according to claim 12, wherein the refrigerant is carbon dioxide.
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