JP2019184115A - Refrigerating machine controller, refrigerating machine, control method of refrigerating machine, and control program of refrigerating machine - Google Patents

Refrigerating machine controller, refrigerating machine, control method of refrigerating machine, and control program of refrigerating machine Download PDF

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JP2019184115A
JP2019184115A JP2018073193A JP2018073193A JP2019184115A JP 2019184115 A JP2019184115 A JP 2019184115A JP 2018073193 A JP2018073193 A JP 2018073193A JP 2018073193 A JP2018073193 A JP 2018073193A JP 2019184115 A JP2019184115 A JP 2019184115A
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control
refrigerant
refrigerant temperature
evaporator
compressor
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JP7154800B2 (en
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恒志 柞磨
Koshi Taruma
恒志 柞磨
政和 甲斐
Masakazu Kai
政和 甲斐
和巳 長田
Kazumi Osada
和巳 長田
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Mitsubishi Heavy Industries Thermal Systems Ltd
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Mitsubishi Heavy Industries Thermal Systems Ltd
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Priority to EP19782212.5A priority patent/EP3760945A4/en
Priority to PCT/JP2019/013853 priority patent/WO2019194082A1/en
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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
    • 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
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/04Refrigeration circuit bypassing means
    • F25B2400/0409Refrigeration circuit bypassing means for the evaporator
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/04Refrigeration circuit bypassing means
    • F25B2400/0411Refrigeration circuit bypassing means for the expansion valve or capillary tube
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/21Refrigerant outlet evaporator temperature
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • 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
    • F25B2700/2117Temperatures of an evaporator
    • F25B2700/21175Temperatures of an evaporator of the refrigerant at the outlet of the evaporator

Abstract

To provide a refrigerating machine controller capable of protecting a discharged refrigerant temperature while suppressing capacity degradation, and to provide a refrigerating machine, and a control method of the refrigerating machine, and a control program of the refrigerating machine.SOLUTION: A controller 10 of a refrigerating machine includes: a compressor 2 compressing a refrigerant; a condenser 3 condensing the compressed refrigerant; an expansion valve 5 expanding a liquid refrigerant, and having an opening controlled by evaporator outlet overheat degree control of controlling a refrigerant overheat degree of the outlet of an evaporator 6 to a value in a first prescribed range; and the evaporator 6 evaporating the refrigerant. The controller stops the evaporator outlet overheat degree control, and controls the opening of the expansion valve 5 in an opening direction by discharged refrigerant temperature protection control of controlling a discharged refrigerant temperature to a value in a second prescribed range, when a discharged refrigerant temperature exceeds a first threshold value, and stops the discharged refrigerant temperature protection control, and controls the opening of the expansion valve 5 by the evaporator outlet overheat degree control, when a discharged refrigerant temperature is lower than a second threshold value smaller than the first threshold value, and a refrigerant overheat degree of the outlet of the evaporator 6 is equal to or more than a third threshold value.SELECTED DRAWING: Figure 2

Description

本発明は、冷凍機の制御装置、冷凍機、冷凍機の制御方法および冷凍機の制御プログラムに関するものである。   The present invention relates to a refrigerator control device, a refrigerator, a refrigerator control method, and a refrigerator control program.

冷凍機は、空調機に比べて、運転時において低圧圧力と高圧圧力との圧力比が大きいことが知られている。冷凍機のように圧力比の大きい運転(高圧力比運転)では、圧縮機の吐出冷媒温度が上がりやすく、吐出冷媒温度が圧縮機の許容温度を超えるような運転条件の場合は、吐出冷媒温度を下げる保護動作が必要となる。
例えば、吐出冷媒温度を下げる保護方法(吐出冷媒温度保護方法)としては、圧縮機の回転数を下げて圧力比を低減する方法、また圧縮機の吸入側へ液冷媒の一部をバイパスして圧縮機を冷却する方法が用いられている。
It is known that the refrigerator has a larger pressure ratio between the low pressure and the high pressure during operation than the air conditioner. In operation with a high pressure ratio (high pressure ratio operation) as in a refrigerator, the discharge refrigerant temperature of the compressor is likely to rise, and the operation is such that the discharge refrigerant temperature exceeds the allowable temperature of the compressor. Protective action to lower
For example, as a protection method for lowering the discharge refrigerant temperature (discharge refrigerant temperature protection method), a method for reducing the pressure ratio by lowering the number of revolutions of the compressor, or by bypassing a part of the liquid refrigerant to the suction side of the compressor A method of cooling the compressor is used.

また、特許文献1には、圧縮機の吐出冷媒温度が目標吐出温度になるまで膨張弁の開度を開方向へ制御することが開示されている。
また特許文献2には、冷媒の過熱度が高い場合は、膨張弁の開度を大きくして冷媒流量を増加させ、吐出冷媒温度が所定の設定値になった場合に冷媒回収運転を終了することが開示されている。
Patent Document 1 discloses that the opening degree of the expansion valve is controlled in the opening direction until the refrigerant discharge temperature of the compressor reaches the target discharge temperature.
Further, in Patent Document 2, when the degree of superheat of the refrigerant is high, the opening of the expansion valve is increased to increase the refrigerant flow rate, and the refrigerant recovery operation is terminated when the discharged refrigerant temperature reaches a predetermined set value. It is disclosed.

国際公開第2015/174054号International Publication No. 2015/174054 特開2000−39237号公報JP 2000-39237 A

しかしながら、上記に開示された圧縮機の回転数を下げる発明及び液冷媒をバイパスする発明では、冷凍能力が大きく低下するという問題があった。
また、特に液冷媒をバイパスする場合は、液冷媒を圧縮機へ戻すため、圧縮機の油が希釈されてしまい潤滑性に影響が及ぶ虞がある。さらに、低圧圧力と高圧圧力との圧力差により液戻し量が変化するため、常に最適な液戻し量に制御することが困難である。
However, the invention disclosed in the above that lowers the rotational speed of the compressor and the invention that bypasses the liquid refrigerant has a problem that the refrigerating capacity is greatly reduced.
In particular, when the liquid refrigerant is bypassed, the liquid refrigerant is returned to the compressor, so that the oil in the compressor is diluted, which may affect the lubricity. Furthermore, since the liquid return amount changes due to the pressure difference between the low pressure and the high pressure, it is difficult to always control the liquid return amount to the optimum amount.

また、上記特許文献1に開示された発明では、膨張弁開度制御における終了条件が開示されておらず、特許文献1に開示された発明のみで冷凍機を制御することは困難である。
一方、上記特許文献2に開示された発明は、圧縮機の吐出冷媒温度を保護する目的の発明ではなく、過熱度をつけて冷媒を増やし、アキュームレータに貯留された余剰冷媒を取り出す発明である。
Moreover, in the invention disclosed in Patent Document 1, the termination condition in the expansion valve opening degree control is not disclosed, and it is difficult to control the refrigerator only with the invention disclosed in Patent Document 1.
On the other hand, the invention disclosed in Patent Document 2 is not an invention for the purpose of protecting the discharge refrigerant temperature of the compressor, but an invention for increasing the refrigerant by increasing the degree of superheat and taking out the excess refrigerant stored in the accumulator.

さらに、上記特許文献1及び2に開示された発明は、いずれも空調機における発明である。冷凍機は、空調機と比較して低圧圧力と高圧圧力との圧力比が大きい運転が行われている。そのため、空調機の制御をそのまま冷凍機の制御に適用することができず、上記特許文献1及び2に開示された発明を、冷凍機の制御に適用することは困難である。   Furthermore, the inventions disclosed in Patent Documents 1 and 2 are both inventions in air conditioners. The refrigerator is operated with a large pressure ratio between the low pressure and the high pressure compared to the air conditioner. For this reason, the control of the air conditioner cannot be applied to the control of the refrigerator as it is, and it is difficult to apply the inventions disclosed in Patent Documents 1 and 2 to the control of the refrigerator.

本発明は、このような事情に鑑みてなされたものであって、能力低下を抑えながら吐出冷媒温度の保護を行うことができる冷凍機の制御装置、冷凍機、冷凍機の制御方法および冷凍機の制御プログラムを提供することを目的とする。   The present invention has been made in view of such circumstances, and has a refrigerator control device, a refrigerator, a refrigerator control method, and a refrigerator capable of protecting the discharged refrigerant temperature while suppressing a decrease in capacity. The purpose is to provide a control program.

上記課題を解決するために、本開示の冷凍機の制御装置、冷凍機、冷凍機の制御方法および冷凍機の制御プログラムは以下の手段を採用する。
本開示の幾つかの実施形態における一態様に係る冷凍機の制御装置は、冷媒を圧縮する圧縮機と、該圧縮機により圧縮された冷媒を凝縮する凝縮器と、該凝縮器から導かれた液冷媒を膨張させるとともに、蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御装置であって、圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御し、圧縮機の吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御する。
In order to solve the above-described problems, a refrigerator control device, a refrigerator, a refrigerator control method, and a refrigerator control program according to the present disclosure employ the following means.
A control device for a refrigerator according to an aspect of some embodiments of the present disclosure includes a compressor that compresses a refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and the condenser. An expansion valve whose degree of opening is controlled by an evaporator outlet superheat degree control that expands the liquid refrigerant and controls the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range, and a refrigerant derived from the expansion valve A control device for a refrigerator including the evaporator, wherein when the refrigerant discharge refrigerant temperature exceeds a first threshold, the evaporator outlet superheat control is stopped, and the refrigerant discharge The opening degree of the expansion valve is controlled in the opening direction by discharge refrigerant temperature protection control for controlling the temperature to a value within a second predetermined range, and the discharge refrigerant temperature of the compressor is less than a second threshold value that is smaller than the first threshold value. And the degree of superheat of the refrigerant at the outlet of the evaporator For more third threshold value, to stop the discharge refrigerant temperature protection control, controls the opening of the expansion valve by the evaporator outlet superheat degree control.

本開示によれば、吐出冷媒温度が第一閾値以下に制御されて圧縮機がほぼ停止することなく連続した運転が可能である。
また、蒸発器に余剰に供給された冷媒の冷媒熱エネルギーが回収されるため、冷凍能力の低下を極めて小さく抑えることができる。
また、圧縮機が冷媒ガス吸入を維持できるため、液冷媒が吸入されず油が希釈しないことから圧縮機の潤滑性に影響が及ぶことがない。
また、膨張弁で冷媒流量を細かく制御できることから、吐出冷媒温度を第一閾値以下に維持するのに必要な最小液戻し量に制御可能であり、安定した運転が可能である。
According to the present disclosure, the discharged refrigerant temperature is controlled to be equal to or lower than the first threshold value, and continuous operation is possible without substantially stopping the compressor.
Moreover, since the refrigerant | coolant thermal energy of the refrigerant | coolant supplied to the evaporator excessively is collect | recovered, the fall of refrigerating capacity can be suppressed very small.
Further, since the compressor can maintain the suction of the refrigerant gas, the liquid refrigerant is not sucked and the oil is not diluted, so that the lubricity of the compressor is not affected.
Further, since the refrigerant flow rate can be finely controlled by the expansion valve, it is possible to control the minimum liquid return amount necessary for maintaining the discharged refrigerant temperature below the first threshold value, and stable operation is possible.

さらに、圧縮機の吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ蒸発器の出口の冷媒過熱度が第三閾値以上の場合は、吐出冷媒温度保護制御を停止し、蒸発器出口過熱度制御によって膨張弁の開度を制御することから、蒸発器の出口の冷媒過熱度が確保されているのを確認した上で、吐出冷媒温度保護制御を終了して通常の蒸発器出口過熱度制御に移行させ、吐出冷媒温度保護制御によって下がりすぎた圧縮機の吐出冷媒温度を上げることができる。
また、吐出冷媒温度保護制御の終了条件が明らかであり、制御を正しく終了させることができる。
Further, when the refrigerant discharge refrigerant temperature is lower than the second threshold value, which is smaller than the first threshold value, and the refrigerant superheat degree at the outlet of the evaporator is equal to or greater than the third threshold value, the discharge refrigerant temperature protection control is stopped. Since the opening degree of the expansion valve is controlled by the evaporator outlet superheat degree control, after confirming that the refrigerant superheat degree at the outlet of the evaporator is secured, the discharge refrigerant temperature protection control is terminated and Shifting to the evaporator outlet superheat degree control, the discharge refrigerant temperature of the compressor that has decreased too much by the discharge refrigerant temperature protection control can be raised.
Further, the end condition of the discharge refrigerant temperature protection control is clear, and the control can be ended correctly.

上記態様では、前記圧縮機の前記吐出冷媒温度が前記第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が前記第三閾値を下回る値である場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を閉方向に制御するとしてもよい。   In the above aspect, when the discharge refrigerant temperature of the compressor is a value lower than the second threshold and the refrigerant superheat degree at the outlet of the evaporator is a value lower than the third threshold, the discharge The refrigerant temperature protection control may be stopped, and the opening degree of the expansion valve may be controlled in the closing direction by the evaporator outlet superheat degree control.

本開示によれば、前記圧縮機の前記吐出冷媒温度が前記第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が前記第三閾値を下回る値である場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を閉方向に制御する。吐出冷媒温度保護制御によって圧縮機の吐出冷媒温度が下がっているとともに、蒸発器の出口の冷媒過熱度が確保すべき値の下限値を下回ることで圧縮機に液バックが生じる可能性がある。しかし、本開示によれば、膨張弁の開度を閉方向に制御するため、蒸発器の出口の冷媒過熱度を高めることができ、さらに圧縮機の吐出冷媒温度を上げることができる。   According to the present disclosure, when the discharge refrigerant temperature of the compressor is a value lower than the second threshold value, and the refrigerant superheat degree at the outlet of the evaporator is a value lower than the third threshold value, The discharge refrigerant temperature protection control is stopped, and the opening degree of the expansion valve is controlled in the closing direction by the evaporator outlet superheat degree control. The discharge refrigerant temperature of the compressor is lowered by the discharge refrigerant temperature protection control, and a liquid back may occur in the compressor when the refrigerant superheat degree at the outlet of the evaporator falls below the lower limit value to be ensured. However, according to the present disclosure, since the opening degree of the expansion valve is controlled in the closing direction, it is possible to increase the refrigerant superheat degree at the outlet of the evaporator and further increase the discharge refrigerant temperature of the compressor.

上記態様では、前記圧縮機の前記吐出冷媒温度が前記第二閾値以上、かつ前記第一閾値以下の値である場合は、前記吐出冷媒温度保護制御による前記膨張弁の開度を保持するように制御するとしてもよい。   In the above aspect, when the discharge refrigerant temperature of the compressor is not less than the second threshold value and not more than the first threshold value, the opening degree of the expansion valve is maintained by the discharge refrigerant temperature protection control. It may be controlled.

本開示によれば、圧縮機の前記吐出冷媒温度が前記第二閾値以上前記第一閾値以下の値である場合は、前記吐出冷媒温度保護制御による前記膨張弁の開度を保持するように制御する。これにより、吐出冷媒温度保護制御において、圧縮機の吐出冷媒温度を第二閾値以上第一閾値以下の第二所定範囲内となるように制御するため、吐出冷媒温度の変動が少なく、安定した運転を継続可能である。また、冷凍機の能力を確保し維持することができる。   According to the present disclosure, when the discharge refrigerant temperature of the compressor is a value that is greater than or equal to the second threshold value and less than or equal to the first threshold value, control is performed to maintain the opening degree of the expansion valve by the discharge refrigerant temperature protection control. To do. Thereby, in the discharge refrigerant temperature protection control, the discharge refrigerant temperature of the compressor is controlled so as to be within the second predetermined range not less than the second threshold and not more than the first threshold. Can be continued. In addition, the capacity of the refrigerator can be secured and maintained.

上記態様では、前記吐出冷媒温度保護制御によって前記膨張弁の開度を制御してから所定時間以上経過した場合、前記圧縮機の前記吐出冷媒温度が前記第一閾値を超えたか否かの判定を行うとしてもよい。   In the above aspect, when a predetermined time or more has elapsed since the opening degree of the expansion valve was controlled by the discharge refrigerant temperature protection control, it is determined whether or not the discharge refrigerant temperature of the compressor has exceeded the first threshold value. It may be done.

本開示によれば、前記吐出冷媒温度保護制御によって前記膨張弁の開度を制御してから所定時間以上経過した場合、前記圧縮機の前記吐出冷媒温度が前記第一閾値を超えたか否かの判定を行う。これにより、所定時間経過し、冷凍機の冷媒回路が定常状態になってから圧縮機の吐出冷媒温度の判定を行うため、正しく判定を行うことができる。   According to the present disclosure, whether or not the discharge refrigerant temperature of the compressor has exceeded the first threshold value when a predetermined time or more has elapsed since the opening degree of the expansion valve was controlled by the discharge refrigerant temperature protection control. Make a decision. Thereby, since the refrigerant | coolant discharge refrigerant | coolant temperature of a compressor is determined after predetermined time passes and the refrigerant circuit of a refrigerator will be in a steady state, it can determine correctly.

上記態様では、前記第三閾値は、前記蒸発器出口過熱度制御における目標冷媒過熱度よりも小さい値であるとしてもよい。   In the above aspect, the third threshold value may be a value smaller than a target refrigerant superheat degree in the evaporator outlet superheat degree control.

本開示によれば、第三閾値は、前記蒸発器出口過熱度制御における目標冷媒過熱度よりも小さい値であることから、蒸発器の出口の冷媒過熱度を最低限確保し、圧縮機の液バックの発生を抑制することができる。   According to the present disclosure, since the third threshold value is smaller than the target refrigerant superheat degree in the evaporator outlet superheat degree control, the minimum refrigerant superheat degree at the outlet of the evaporator is ensured, and the compressor liquid The occurrence of back can be suppressed.

本開示の幾つかの実施形態における一態様に係る冷凍機は、冷媒を圧縮する圧縮機と、該圧縮機により圧縮された冷媒を凝縮する凝縮器と、該凝縮器から導かれた液冷媒を膨張させるとともに、前記蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、前述したいずれかの制御装置と、を備える。   A refrigerator according to an aspect of some embodiments of the present disclosure includes a compressor that compresses a refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and a liquid refrigerant guided from the condenser. An expansion valve whose degree of opening is controlled by an evaporator outlet superheat degree control that controls the degree of refrigerant superheat at the outlet of the evaporator to a value within a first predetermined range, and the refrigerant introduced from the expansion valve evaporates The evaporator to be operated, and any one of the control devices described above.

本開示の幾つかの実施形態における一態様に係る冷凍機の制御方法は、冷媒を圧縮する圧縮機と、該圧縮機により圧縮された冷媒を凝縮する凝縮器と、該凝縮器から導かれた液冷媒を膨張させるとともに、前記蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御方法であって、圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御する工程と、圧縮機の吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御する工程と、を有する。   A method of controlling a refrigerator according to an aspect of some embodiments of the present disclosure is provided with a compressor that compresses a refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and the condenser. An expansion valve whose degree of opening is controlled by an evaporator outlet superheat degree control for expanding the liquid refrigerant and controlling the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range, and led from the expansion valve A control method of a refrigerator comprising the evaporator for evaporating a refrigerant, and when the discharge refrigerant temperature of the compressor exceeds a first threshold, the evaporator outlet superheat degree control is stopped, and the discharge A step of controlling the opening of the expansion valve in the opening direction by discharge refrigerant temperature protection control for controlling the refrigerant temperature to a value within a second predetermined range; and a second threshold value at which the discharge refrigerant temperature of the compressor is lower than the first threshold value. Before the evaporator outlet. If the refrigerant superheating degree is equal to or greater than the third threshold value, to stop the discharge refrigerant temperature protection control, and a step of controlling an opening degree of the expansion valve by the evaporator outlet superheat degree control.

本開示の幾つかの実施形態における一態様に係る冷凍機の制御プログラムは、冷媒を圧縮する圧縮機と、該圧縮機により圧縮された冷媒を凝縮する凝縮器と、該凝縮器から導かれた液冷媒を膨張させるとともに、前記蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御プログラムであって、圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御するステップと、圧縮機の吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御するステップと、を有する。   A control program for a refrigerator according to an aspect of some embodiments of the present disclosure is derived from a compressor that compresses a refrigerant, a condenser that condenses the refrigerant compressed by the compressor, and the condenser. An expansion valve whose degree of opening is controlled by an evaporator outlet superheat degree control for expanding the liquid refrigerant and controlling the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range, and led from the expansion valve A control program for a refrigerator comprising the evaporator for evaporating the refrigerant, and when the discharge refrigerant temperature of the compressor exceeds a first threshold, the evaporator outlet superheat degree control is stopped and the discharge A step of controlling the opening of the expansion valve in the opening direction by discharge refrigerant temperature protection control for controlling the refrigerant temperature to a value within a second predetermined range; and a second threshold value at which the discharge refrigerant temperature of the compressor is smaller than the first threshold value. And a value below When the refrigerant superheat degree at the outlet of the generator is equal to or greater than a third threshold, the discharge refrigerant temperature protection control is stopped, and the opening degree of the expansion valve is controlled by the evaporator outlet superheat degree control. .

本開示によれば、吐出冷媒温度が第一閾値を超えた場合は蒸発器出口過熱度制御を停止し吐出冷媒温度保護制御によって膨張弁の開度を制御するので、吐出冷媒温度を下げる保護動作を実施することができる。
また、圧縮機の吐出冷媒温度が第二閾値を下回る値であり、かつ、蒸発器の出口の冷媒過熱度が第三閾値以上の場合は、吐出冷媒温度保護制御を停止し、蒸発器出口過熱度制御によって膨張弁の開度を制御するので、吐出冷媒温度保護制御の終了条件が明らかであり、正しく停止することができる。
According to the present disclosure, when the discharge refrigerant temperature exceeds the first threshold value, the evaporator outlet superheat degree control is stopped, and the opening degree of the expansion valve is controlled by the discharge refrigerant temperature protection control. Can be implemented.
Also, when the refrigerant discharge refrigerant temperature is lower than the second threshold value and the refrigerant superheat degree at the evaporator outlet is equal to or higher than the third threshold value, the discharge refrigerant temperature protection control is stopped and the evaporator outlet overheat is stopped. Since the degree of opening of the expansion valve is controlled by the degree control, the end condition of the discharged refrigerant temperature protection control is clear and can be stopped correctly.

幾つかの実施形態に係る冷凍機の冷凍サイクルの一態様を示した概略構成図である。It is the schematic block diagram which showed the one aspect | mode of the refrigerating cycle of the refrigerator which concerns on some embodiment. 幾つかの実施形態に係る冷凍機の制御装置の制御を示したフローチャートである。It is the flowchart which showed control of the control apparatus of the refrigerator which concerns on some embodiment. 参考例としての冷凍機の冷凍サイクルを示した概略構成図である。It is the schematic block diagram which showed the refrigerating cycle of the refrigerator as a reference example. 参考例としての冷凍機における吐出冷媒温度の変化を示したグラフである。It is the graph which showed the change of the discharge refrigerant | coolant temperature in the refrigerator as a reference example. 幾つかの実施形態に係る冷凍機における吐出冷媒温度の変化を示したグラフである。It is the graph which showed the change of the discharge refrigerant | coolant temperature in the refrigerator which concerns on some embodiment. 参考例としての冷凍機における冷凍能力の変化を示したグラフである。It is the graph which showed the change of the refrigerating capacity in the refrigerator as a reference example. 幾つかの実施形態に係る冷凍機における冷凍能力の変化を示したグラフである。It is the graph which showed the change of the refrigerating capacity in the refrigerator concerning some embodiments. 参考例としての冷凍機における圧力−エンタルピ線図である。It is a pressure-enthalpy diagram in the refrigerator as a reference example. 幾つかの実施形態に係る冷凍機における圧力−エンタルピ線図である。It is a pressure-enthalpy diagram in the refrigerator concerning some embodiments.

以下に、本開示の幾つかの実施形態に係る冷凍機の制御装置、冷凍機、冷凍機の制御方法および冷凍機の制御プログラムの各実施形態について、図面を参照して説明する。
図1には、本開示の幾つかの実施形態に係る冷凍機の冷凍サイクルの一態様の概略構成が示されている。
図1に示されるように、冷凍機の冷凍サイクル1は、蒸発器6から導かれた冷媒ガスを圧縮する圧縮機2と、圧縮機2から送られる圧縮機2により圧縮された高温高圧の冷媒ガスを外気と熱交換させて凝縮する凝縮器3と、凝縮器3から送られる凝縮器3で凝縮された液冷媒を蒸発器6からのガス冷媒と熱交換させて過冷却する気液内部熱交換器(熱交換器)4と、気液内部熱交換器4から導かれる過冷却された液冷媒を膨張させる膨張弁5と、膨張された冷媒と空気とを熱交換させて冷媒を蒸発させる蒸発器6と、をこの順に冷媒配管8により接続して構成されている。蒸発器6は、冷凍庫内を冷却するために用いられる。
Hereinafter, embodiments of a refrigerator control device, a refrigerator, a refrigerator control method, and a refrigerator control program according to some embodiments of the present disclosure will be described with reference to the drawings.
FIG. 1 shows a schematic configuration of one aspect of a refrigeration cycle of a refrigerator according to some embodiments of the present disclosure.
As shown in FIG. 1, a refrigeration cycle 1 of a refrigerator includes a compressor 2 that compresses a refrigerant gas introduced from an evaporator 6, and a high-temperature and high-pressure refrigerant compressed by the compressor 2 that is sent from the compressor 2. The condenser 3 that condenses the gas by heat exchange with the outside air, and the gas-liquid internal heat that supercools the liquid refrigerant condensed in the condenser 3 sent from the condenser 3 with the gas refrigerant from the evaporator 6. An exchanger (heat exchanger) 4, an expansion valve 5 for expanding the supercooled liquid refrigerant guided from the gas-liquid internal heat exchanger 4, and the expanded refrigerant and air are heat-exchanged to evaporate the refrigerant. The evaporator 6 is connected to the evaporator pipe 8 in this order. The evaporator 6 is used for cooling the inside of the freezer.

冷凍サイクル1には、圧縮機2から吐出される冷媒温度(吐出冷媒温度)を検出する吐出冷媒温度センサ7が設けられており、吐出冷媒温度センサ7の検出値は、制御装置10に入力されるように構成されている。   The refrigeration cycle 1 is provided with a discharge refrigerant temperature sensor 7 that detects a refrigerant temperature (discharge refrigerant temperature) discharged from the compressor 2, and a detection value of the discharge refrigerant temperature sensor 7 is input to the control device 10. It is comprised so that.

制御装置10は、蒸発器6出口の冷媒過熱度を目標冷媒過熱度を含む第一所定範囲の値に制御するように膨張弁5の開度を調整する機能を有している。
蒸発器6出口の冷媒過熱度を確保することで、蒸発器6を効率よく使用することができる。そこで、冷媒過熱度の制御目標値である目標冷媒過熱度を設定する。制御装置10は、蒸発器6出口の冷媒過熱度が目標冷媒過熱度を含む第一所定範囲の値となるように制御する。
冷媒過熱度の制御は、制御装置10が膨張弁5の開度を調整することで行われる。例えば、冷媒過熱度を上げる場合は、膨張弁5の開度は閉方向に制御される。また冷媒過熱度を下げる場合は、膨張弁5の開度は開方向に制御される。
例えば、目標冷媒過熱度は7℃である。
The control device 10 has a function of adjusting the opening degree of the expansion valve 5 so as to control the refrigerant superheat degree at the outlet of the evaporator 6 to a value within a first predetermined range including the target refrigerant superheat degree.
By securing the refrigerant superheat degree at the outlet of the evaporator 6, the evaporator 6 can be used efficiently. Therefore, a target refrigerant superheat degree that is a control target value of the refrigerant superheat degree is set. The control device 10 performs control so that the refrigerant superheat degree at the outlet of the evaporator 6 becomes a value in a first predetermined range including the target refrigerant superheat degree.
Control of the degree of refrigerant superheat is performed by the control device 10 adjusting the opening of the expansion valve 5. For example, when increasing the degree of refrigerant superheat, the opening of the expansion valve 5 is controlled in the closing direction. When the refrigerant superheat degree is lowered, the opening degree of the expansion valve 5 is controlled in the opening direction.
For example, the target refrigerant superheat degree is 7 ° C.

制御装置10は、例えば、CPU(Central Processing Unit)、RAM(Random Access Memory)、ROM(Read Only Memory)、及びコンピュータ読み取り可能な非一時的な記憶媒体等から構成されている。そして、各種機能を実現するための一連の処理は、一例として、プログラムの形式で記憶媒体等に記憶されており、このプログラムをCPUがRAM等に読み出して、情報の加工・演算処理を実行することにより、各種機能が実現される。なお、プログラムは、ROMやその他の記憶媒体に予めインストールしておく形態や、コンピュータ読み取り可能な記憶媒体に記憶された状態で提供される形態、有線又は無線による通信手段を介して配信される形態等が適用されてもよい。コンピュータ読み取り可能な記憶媒体とは、磁気ディスク、光磁気ディスク、CD−ROM、DVD−ROM、半導体メモリ等である。   The control device 10 includes, for example, a CPU (Central Processing Unit), a RAM (Random Access Memory), a ROM (Read Only Memory), and a computer-readable non-transitory storage medium. A series of processes for realizing various functions is stored in a storage medium or the like in the form of a program as an example, and the CPU reads the program into a RAM or the like to execute information processing / arithmetic processing. As a result, various functions are realized. The program is preinstalled in a ROM or other storage medium, provided in a state stored in a computer-readable storage medium, or distributed via wired or wireless communication means. Etc. may be applied. The computer-readable storage medium is a magnetic disk, a magneto-optical disk, a CD-ROM, a DVD-ROM, a semiconductor memory, or the like.

冷凍機は、空調機に比べて、運転時における低圧圧力と高圧圧力との圧力比が大きいとされている。このように圧力比の大きい高圧力比運転では、圧縮機2の吐出冷媒温度が上がりやすい。
一方で、圧縮機2には運転が可能な温度に上限があり、これを圧縮機許容温度上限値としている。そこで、吐出冷媒温度センサ7が計測する吐出冷媒温度が圧縮機2の圧縮機許容温度上限値を超えるような運転条件の場合は、吐出冷媒温度を下げる保護動作が必要となる。
The refrigerator is said to have a larger pressure ratio between the low pressure and the high pressure during operation than the air conditioner. In such a high pressure ratio operation with a large pressure ratio, the discharge refrigerant temperature of the compressor 2 is likely to rise.
On the other hand, the compressor 2 has an upper limit on the temperature at which the compressor 2 can be operated, and this is set as the compressor allowable temperature upper limit. Therefore, when the operating condition is such that the discharged refrigerant temperature measured by the discharged refrigerant temperature sensor 7 exceeds the compressor allowable temperature upper limit value of the compressor 2, a protection operation for lowering the discharged refrigerant temperature is required.

ここで、吐出冷媒温度が圧縮機許容温度上限値に到達してしまうと、圧縮機2は運転停止するだけでなく故障に至る虞がある。そこで、圧縮機許容温度上限値よりも所定温度低い吐出冷媒温度制御上限値(第一閾値)を設けることとする。吐出冷媒温度が吐出冷媒温度制御上限値に到達すると、本開示の幾つかの実施形態では吐出冷媒温度保護制御を行うとする。吐出冷媒温度制御上限値は、例えば圧縮機許容温度上限値−15℃である。   Here, when the discharged refrigerant temperature reaches the upper limit value of the compressor allowable temperature, the compressor 2 may not only stop operation but also cause failure. Therefore, a discharge refrigerant temperature control upper limit value (first threshold value) lower by a predetermined temperature than the compressor allowable temperature upper limit value is provided. When the discharge refrigerant temperature reaches the discharge refrigerant temperature control upper limit, it is assumed that discharge refrigerant temperature protection control is performed in some embodiments of the present disclosure. The discharge refrigerant temperature control upper limit value is, for example, the compressor allowable temperature upper limit value −15 ° C.

また、吐出冷媒温度制御上限値よりも小さい第二閾値として、吐出冷媒温度制御下限値を設ける。吐出冷媒温度制御下限値は、例えば吐出冷媒温度制御上限値−35℃である。吐出冷媒温度制御下限値は、吐出冷媒温度が吐出冷媒温度制御下限値を下回ると圧縮機2の温度が下がりすぎていると判断し、圧縮機2の温度を上昇させる目安となる温度である。   In addition, a discharge refrigerant temperature control lower limit value is provided as a second threshold value that is smaller than the discharge refrigerant temperature control upper limit value. The discharge refrigerant temperature control lower limit value is, for example, the discharge refrigerant temperature control upper limit value −35 ° C. The discharge refrigerant temperature control lower limit value is a temperature that is a guideline for determining that the temperature of the compressor 2 is too low when the discharge refrigerant temperature falls below the discharge refrigerant temperature control lower limit value, and increasing the temperature of the compressor 2.

吐出冷媒温度保護制御は、吐出冷媒温度を第二所定範囲の値となるように制御するものである。第二所定範囲は、吐出冷媒温度制御下限値(第二閾値)以上吐出冷媒温度制御上限値(第一閾値)以下の範囲である。吐出冷媒温度センサ7が計測する吐出冷媒温度が第二所定範囲の値となるように、制御装置10が膨張弁5の開度を制御する。ここで、吐出冷媒温度制御下限値は、吐出冷媒温度制御上限値よりも小さい値である。   The discharge refrigerant temperature protection control is to control the discharge refrigerant temperature to be a value in the second predetermined range. The second predetermined range is a range not less than the discharge refrigerant temperature control lower limit (second threshold) and not more than the discharge refrigerant temperature control upper limit (first threshold). The control device 10 controls the opening degree of the expansion valve 5 so that the discharge refrigerant temperature measured by the discharge refrigerant temperature sensor 7 falls within a second predetermined range. Here, the discharge refrigerant temperature control lower limit value is a value smaller than the discharge refrigerant temperature control upper limit value.

以下に、本開示の幾つかの実施形態に係る冷凍機の制御について説明する。
図2には、本開示の幾つかの実施形態に係る冷凍機の制御装置の制御がフローチャートに示されている。
制御装置10の制御が開始されると、圧縮機吐出冷媒温度(Td)保護制御が行われているか否かの判定を行う(S201)。圧縮機吐出冷媒温度保護制御が行われていると判定された場合は、ステップS202へ遷移し、行われていないと判定された場合はステップS208へ遷移する。
Below, control of the refrigerator concerning some embodiments of this indication is explained.
FIG. 2 is a flowchart showing the control of the refrigerator control device according to some embodiments of the present disclosure.
When the control of the control device 10 is started, it is determined whether or not the compressor discharge refrigerant temperature (Td) protection control is being performed (S201). When it is determined that the compressor discharge refrigerant temperature protection control is being performed, the process proceeds to step S202, and when it is determined that the compressor discharge refrigerant temperature protection control is not being performed, the process proceeds to step S208.

ステップS202では、前回の処理にて、膨張弁5の開度を変更した後に所定時間以上経過したか否かの判定を行う。膨張弁5の開度を変更すると、冷凍サイクル1の冷媒回路が定常状態になるまでタイムラグが生じる。そのため、冷媒回路が定常状態になったと予測される時間を所定時間に設定し、この所定時間が経過したかどうかの判定が行われる。
開度変更後に所定時間以上経過している場合はステップS203へ遷移し、所定時間が経過していない場合は一旦処理が終了し、再度初めから処理が行われる。
In step S202, it is determined whether or not a predetermined time has elapsed since the opening of the expansion valve 5 was changed in the previous process. When the opening degree of the expansion valve 5 is changed, a time lag occurs until the refrigerant circuit of the refrigeration cycle 1 reaches a steady state. Therefore, the time when the refrigerant circuit is predicted to be in a steady state is set to a predetermined time, and it is determined whether or not the predetermined time has elapsed.
When the predetermined time or more has elapsed after the opening degree change, the process proceeds to step S203, and when the predetermined time has not elapsed, the process is once ended and the process is performed again from the beginning.

ステップS202において、膨張弁5の開度を変更した後に所定時間以上経過したと判定された場合は、吐出冷媒温度センサ7の検出値である圧縮機吐出冷媒温度が吐出冷媒温度制御上限値(第一閾値)を上回るか否かの判定が行われる(S203)。   If it is determined in step S202 that a predetermined time or more has elapsed after the opening degree of the expansion valve 5 is changed, the compressor discharge refrigerant temperature detected by the discharge refrigerant temperature sensor 7 is set to the discharge refrigerant temperature control upper limit value (first value). It is determined whether or not the threshold value is exceeded (S203).

ステップS203において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値を上回ると判定された場合は、ステップS210へ遷移する。一方、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値以下であると判定された場合は、ステップS204へ遷移する。   When it is determined in step S203 that the compressor discharge refrigerant temperature exceeds the discharge refrigerant temperature control upper limit value, the process proceeds to step S210. On the other hand, when it is determined that the compressor discharge refrigerant temperature is equal to or lower than the discharge refrigerant temperature control upper limit value, the process proceeds to step S204.

ステップS203において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値を上回ると判定された場合は、膨張弁5の開度を所定量増加させる(S210)。すなわち、制御装置10は、膨張弁5の開度を所定量だけ開方向に制御する。これにより、冷凍サイクル1を循環する冷媒流量が増加し、圧縮機吐出冷媒温度が下がることとなる。この場合、蒸発器6の出口の冷媒過熱度も下がる。   If it is determined in step S203 that the compressor discharge refrigerant temperature exceeds the discharge refrigerant temperature control upper limit, the opening of the expansion valve 5 is increased by a predetermined amount (S210). That is, the control device 10 controls the opening degree of the expansion valve 5 in the opening direction by a predetermined amount. Thereby, the refrigerant | coolant flow volume which circulates through the refrigerating cycle 1 increases, and the compressor discharge refrigerant temperature falls. In this case, the refrigerant superheat degree at the outlet of the evaporator 6 also decreases.

ステップS210において膨張弁5の開度が所定量増加されると、一旦処理が終了し、再度初めから処理が行われる。   When the opening degree of the expansion valve 5 is increased by a predetermined amount in step S210, the process is once ended, and the process is performed again from the beginning.

一方ステップS203において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値以下であると判定された場合は、圧縮機吐出冷媒温度が吐出冷媒温度制御下限値(第二閾値)以上か否かの判定が行われる(S204)。   On the other hand, if it is determined in step S203 that the compressor discharge refrigerant temperature is equal to or lower than the discharge refrigerant temperature control upper limit value, it is determined whether or not the compressor discharge refrigerant temperature is equal to or higher than the discharge refrigerant temperature control lower limit value (second threshold value). Is performed (S204).

ステップS204において、圧縮機吐出冷媒温度が吐出冷媒温度制御下限値以上であると判定された場合は、膨張弁5の開度を保持するように制御が行われたまま一旦処理が終了し、再度初めから処理が行われる。   In step S204, when it is determined that the compressor discharge refrigerant temperature is equal to or higher than the discharge refrigerant temperature control lower limit value, the process is temporarily terminated while the control is performed so as to maintain the opening degree of the expansion valve 5, and again, Processing is performed from the beginning.

一方ステップS204において、圧縮機吐出冷媒温度が吐出冷媒温度制御下限値を下回ると判定された場合は、ステップS205へ遷移する。   On the other hand, when it is determined in step S204 that the compressor discharge refrigerant temperature is lower than the discharge refrigerant temperature control lower limit value, the process proceeds to step S205.

圧縮機吐出冷媒温度が吐出冷媒温度制御下限値を下回る場合は、圧縮機吐出冷媒温度を上昇させる必要がある。ここで、ステップS205においては、蒸発器6の出口における冷媒過熱度の判定が行われる。蒸発器6の出口における冷媒過熱度が冷媒過熱度制御下限値(第三閾値)以上であると判定された場合は、ステップS206へ遷移する。一方、冷媒過熱度が冷媒過熱度制御下限値を下回ると判定された場合は、ステップS211へ遷移する。
ここで、冷媒過熱度制御下限値(第三閾値)は、蒸発器6を効率良く使用するために、蒸発器6出口の冷媒過熱度において最低限確保すべき値である。冷媒過熱度制御下限値は、目標冷媒過熱度よりも小さい値であり、例えば目標冷媒過熱度−2℃が設定される。
When the compressor discharge refrigerant temperature is lower than the discharge refrigerant temperature control lower limit value, it is necessary to increase the compressor discharge refrigerant temperature. Here, in step S205, the degree of refrigerant superheat at the outlet of the evaporator 6 is determined. When it is determined that the refrigerant superheat degree at the outlet of the evaporator 6 is equal to or higher than the refrigerant superheat degree control lower limit (third threshold value), the process proceeds to step S206. On the other hand, when it determines with a refrigerant | coolant superheat degree being less than a refrigerant | coolant superheat degree control lower limit, it changes to step S211.
Here, the refrigerant superheat degree control lower limit value (third threshold value) is a value that should be secured at least in the refrigerant superheat degree at the outlet of the evaporator 6 in order to use the evaporator 6 efficiently. The refrigerant superheat degree control lower limit value is a value smaller than the target refrigerant superheat degree, for example, a target refrigerant superheat degree of −2 ° C. is set.

圧縮機吐出冷媒温度が吐出冷媒温度制御下限値を下回り(S204でNO)、かつ、蒸発器6の出口における冷媒過熱度が冷媒過熱度制御下限値以上であると判定された場合(S205でYES)は、圧縮機吐出冷媒温度を上げる必要があるが、冷媒過熱度は確保されていることから、圧縮機吐出冷媒温度保護制御を終了し(S206)、蒸発器出口過熱度制御を行う(S207)。
ステップS207において蒸発器出口過熱度制御が開始されると、一旦処理が終了し、再度初めから処理が行われる。
When it is determined that the compressor discharge refrigerant temperature is lower than the discharge refrigerant temperature control lower limit value (NO in S204) and the refrigerant superheat degree at the outlet of the evaporator 6 is equal to or higher than the refrigerant superheat degree control lower limit value (YES in S205) ) Needs to increase the refrigerant discharge refrigerant temperature, but since the refrigerant superheat degree is secured, the compressor discharge refrigerant temperature protection control is terminated (S206), and the evaporator outlet superheat degree control is performed (S207). ).
When the evaporator outlet superheat degree control is started in step S207, the process is once ended, and the process is performed again from the beginning.

一方、圧縮機吐出冷媒温度が吐出冷媒温度制御下限値を下回り(S204でNO)、かつ、蒸発器6の出口における冷媒過熱度が冷媒過熱度制御下限値を下回ると判定された場合(S205でNO)は、圧縮機吐出冷媒温度及び冷媒過熱度を上げる必要がある。膨張弁5の開度を大きくすると、蒸発器6の出口における冷媒過熱度が付かなくなる場合がある。この時、圧縮機2に液バックが生じる可能性があることから、冷媒過熱度を確保しておく必要がある。そこで、膨張弁5の開度を所定量減少させることとする(S211)。すなわち、制御装置10は、膨張弁5の開度を所定量だけ閉方向に制御する。これにより、冷凍サイクル1を循環する冷媒流量が減少し、圧縮機吐出冷媒温度および蒸発器6の出口における冷媒過熱度が上がる。
ステップS211において膨張弁5の開度が所定量減少されると、一旦処理が終了し、再度初めから処理が行われる。
以上のようにして、圧縮機吐出冷媒温度保護制御が行われる。
On the other hand, when it is determined that the compressor discharge refrigerant temperature is lower than the discharge refrigerant temperature control lower limit value (NO in S204) and the refrigerant superheat degree at the outlet of the evaporator 6 is lower than the refrigerant superheat degree control lower limit value (S205). NO) needs to increase the compressor discharge refrigerant temperature and the degree of refrigerant superheat. When the opening degree of the expansion valve 5 is increased, the refrigerant superheat degree at the outlet of the evaporator 6 may not be applied. At this time, since a liquid back may occur in the compressor 2, it is necessary to ensure the degree of refrigerant superheat. Therefore, the opening degree of the expansion valve 5 is decreased by a predetermined amount (S211). That is, the control device 10 controls the opening degree of the expansion valve 5 in the closing direction by a predetermined amount. Thereby, the refrigerant | coolant flow rate which circulates through the refrigerating cycle 1 reduces, and the refrigerant | coolant discharge refrigerant | coolant temperature and the refrigerant | coolant superheat degree in the exit of the evaporator 6 rise.
When the opening degree of the expansion valve 5 is decreased by a predetermined amount in step S211, the process is once ended and the process is performed again from the beginning.
The compressor discharge refrigerant temperature protection control is performed as described above.

また、ステップS201において、圧縮機吐出冷媒温度保護制御が行われていないと判定された場合は、吐出冷媒温度センサ7の検出値である圧縮機吐出冷媒温度が吐出冷媒温度制御上限値(第一閾値)を上回るか否かの判定が行われる(S208)。   If it is determined in step S201 that the compressor discharge refrigerant temperature protection control is not performed, the compressor discharge refrigerant temperature detected by the discharge refrigerant temperature sensor 7 is the discharge refrigerant temperature control upper limit value (first value). It is determined whether or not the threshold value is exceeded (S208).

ステップS208において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値を上回ると判定された場合は、ステップS209へ遷移する。一方、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値以下であると判定された場合は、ステップS207へ遷移する。   When it is determined in step S208 that the compressor discharge refrigerant temperature exceeds the discharge refrigerant temperature control upper limit value, the process proceeds to step S209. On the other hand, when it is determined that the compressor discharge refrigerant temperature is equal to or lower than the discharge refrigerant temperature control upper limit value, the process proceeds to step S207.

ステップS208において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値を上回ると判定された場合は、圧縮機吐出冷媒温度保護制御を開始し(S209)、膨張弁5の開度を所定量増加させる(S210)。すなわち、制御装置10は、膨張弁5の開度を所定量だけ開方向に制御する。これにより、冷凍サイクル1を循環する冷媒流量が増加し、圧縮機吐出冷媒温度が下がることとなる。この場合、蒸発器6の出口の冷媒過熱度も下がる。   If it is determined in step S208 that the compressor discharge refrigerant temperature exceeds the discharge refrigerant temperature control upper limit, compressor discharge refrigerant temperature protection control is started (S209), and the opening degree of the expansion valve 5 is increased by a predetermined amount. (S210). That is, the control device 10 controls the opening degree of the expansion valve 5 in the opening direction by a predetermined amount. Thereby, the refrigerant | coolant flow volume which circulates through the refrigerating cycle 1 increases, and the compressor discharge refrigerant temperature falls. In this case, the refrigerant superheat degree at the outlet of the evaporator 6 also decreases.

ステップS210において膨張弁5の開度が所定量増加されると、一旦処理が終了し、再度初めから処理が行われる。   When the opening degree of the expansion valve 5 is increased by a predetermined amount in step S210, the process is once ended, and the process is performed again from the beginning.

一方ステップS208において、圧縮機吐出冷媒温度が吐出冷媒温度制御上限値以下であると判定された場合は、蒸発器出口過熱度制御を行う(S207)。
ステップS207において蒸発器出口過熱度制御が開始されると、一旦処理が終了し、再度初めから処理が行われる。
このように、通常の蒸発器出口過熱度制御を行っている場合は、図2のフローチャートにおいてステップS201、ステップS208、ステップS207の順で遷移することとなる。
On the other hand, when it is determined in step S208 that the compressor discharge refrigerant temperature is equal to or lower than the discharge refrigerant temperature control upper limit value, the evaporator outlet superheat degree control is performed (S207).
When the evaporator outlet superheat degree control is started in step S207, the process is once ended, and the process is performed again from the beginning.
As described above, when normal evaporator outlet superheat control is performed, the process proceeds in the order of step S201, step S208, and step S207 in the flowchart of FIG.

以下に、参考例としての冷凍機と比較して、本開示の幾つかの実施形態に係る冷凍機の制御装置による制御について説明する。参考例としての冷凍機の冷凍サイクル51は、図3に示されるように、凝縮器53の出口側と圧縮機52の入口側とを接続する液バイパスライン59を備えている。参考例としての冷凍機は、吐出冷媒温度センサ57が計測する圧縮機52の吐出冷媒温度が吐出冷媒温度制御上限値を超える場合に、圧縮機52の入口側へ液冷媒をバイパスするように液バイパス制御を行うことで圧縮機52を冷却する。   Below, compared with the refrigerator as a reference example, control by the control device of the refrigerator concerning some embodiments of this indication is explained. The refrigeration cycle 51 of the refrigerator as a reference example includes a liquid bypass line 59 that connects the outlet side of the condenser 53 and the inlet side of the compressor 52, as shown in FIG. The refrigerating machine as a reference example is configured to bypass the liquid refrigerant to the inlet side of the compressor 52 when the discharge refrigerant temperature of the compressor 52 measured by the discharge refrigerant temperature sensor 57 exceeds the discharge refrigerant temperature control upper limit value. The compressor 52 is cooled by performing bypass control.

参考例としての冷凍機の他の構成は、本開示の幾つかの実施形態に係る冷凍機と同様であり、それぞれ圧縮機2と圧縮機52、凝縮器3と凝縮器53、気液内部熱交換器4と気液内部熱交換器54、膨張弁5と膨張弁55、蒸発器6と蒸発器56、吐出冷媒温度センサ7と吐出冷媒温度センサ57、冷媒配管8と冷媒配管58、とがそれぞれ対応している。
また、制御装置50は、液バイパス制御を行う。
Other configurations of the refrigerator as a reference example are the same as those of the refrigerator according to some embodiments of the present disclosure, and the compressor 2 and the compressor 52, the condenser 3 and the condenser 53, and the gas-liquid internal heat, respectively. The exchanger 4 and the gas-liquid internal heat exchanger 54, the expansion valve 5 and the expansion valve 55, the evaporator 6 and the evaporator 56, the discharge refrigerant temperature sensor 7 and the discharge refrigerant temperature sensor 57, the refrigerant pipe 8 and the refrigerant pipe 58, Each corresponds.
The control device 50 performs liquid bypass control.

図4は、参考例としての冷凍機における吐出冷媒温度の変化を示したグラフである。
図4において、縦軸は圧縮機52からの吐出冷媒温度、横軸は時間である。また、吐出冷媒温度において、aは後述する液バイパス制御終了温度、bは吐出冷媒温度制御上限値、cは圧縮機許容温度上限値を示す。
FIG. 4 is a graph showing changes in the discharged refrigerant temperature in a refrigerator as a reference example.
In FIG. 4, the vertical axis represents the temperature of refrigerant discharged from the compressor 52, and the horizontal axis represents time. Moreover, in discharge refrigerant temperature, a shows liquid bypass control end temperature mentioned later, b shows discharge refrigerant temperature control upper limit, c shows compressor allowable temperature upper limit.

図4の時間0から時間が経過すると、圧縮機52の吐出冷媒温度は上昇し、時間t1において吐出冷媒温度制御上限値bに到達する。吐出冷媒温度が吐出冷媒温度制御上限値bに到達すると、制御装置50により液バイパス制御が開始され、液バイパスライン59が開かれる。液バイパス制御が開始されてから圧縮機52の吐出冷媒温度が下がり始めるにはタイムラグがあるため、時間t1を過ぎて一定時間経過後、吐出冷媒温度は下がり始める。液バイパス制御には終了温度が設定されており、これを液バイパス制御終了温度aとする。時間t2において、吐出冷媒温度が液バイパス制御終了温度aに到達すると、液バイパスライン59が閉じられ、液バイパス制御が終了する。   When time elapses from time 0 in FIG. 4, the discharge refrigerant temperature of the compressor 52 rises, and reaches the discharge refrigerant temperature control upper limit b at time t1. When the discharge refrigerant temperature reaches the discharge refrigerant temperature control upper limit b, the liquid bypass control is started by the control device 50 and the liquid bypass line 59 is opened. Since there is a time lag for the discharge refrigerant temperature of the compressor 52 to start decreasing after the liquid bypass control is started, the discharge refrigerant temperature starts to decrease after a lapse of a certain time after the time t1. An end temperature is set for the liquid bypass control, and this is set as the liquid bypass control end temperature a. When the discharged refrigerant temperature reaches the liquid bypass control end temperature a at time t2, the liquid bypass line 59 is closed, and the liquid bypass control ends.

液バイパス制御が終了されてから、圧縮機52の吐出冷媒温度が上がり始める場合にもタイムラグがあるため、時間t2を過ぎて一定時間経過後、吐出冷媒温度は上がり始める。その後、吐出冷媒温度が時間t3に吐出冷媒温度制御上限値bに到達すると液バイパス制御が開始され、時間t4に液バイパス制御終了温度aに到達すると液バイパス制御が終了されるように、液バイパス制御の開始と終了が交互に連続して行われる。   Since there is a time lag even when the discharge refrigerant temperature of the compressor 52 starts to rise after the liquid bypass control is finished, the discharge refrigerant temperature starts to rise after a lapse of a certain time after the time t2. Thereafter, the liquid bypass control is started when the discharge refrigerant temperature reaches the discharge refrigerant temperature control upper limit b at time t3, and the liquid bypass control is ended when the liquid bypass control end temperature a is reached at time t4. The start and end of control are performed alternately and continuously.

図4に示されるように、液バイパス制御が行われる場合は、吐出冷媒温度の温度変化が大きい。そのため、吐出冷媒温度が吐出冷媒温度制御上限値b及び液バイパス制御終了温度aに頻繁に到達し、短時間で制御が切り替わることとなる。また、液冷媒が凝縮器53の出口から圧縮機52の入口へバイパスされるため、蒸発器56に流入する冷媒量が少なくなり、減少した冷媒量の分だけ冷凍機能に寄与しないこととなる。   As shown in FIG. 4, when the liquid bypass control is performed, the temperature change of the discharged refrigerant temperature is large. Therefore, the discharge refrigerant temperature frequently reaches the discharge refrigerant temperature control upper limit b and the liquid bypass control end temperature a, and the control is switched in a short time. Further, since the liquid refrigerant is bypassed from the outlet of the condenser 53 to the inlet of the compressor 52, the amount of refrigerant flowing into the evaporator 56 is reduced and does not contribute to the refrigeration function by the reduced amount of refrigerant.

図5は、本開示の幾つかの実施形態に係る冷凍機における吐出冷媒温度の変化を示したグラフである。
図5において、縦軸は圧縮機52からの吐出冷媒温度、横軸は時間である。また、吐出冷媒温度において、dは後述する吐出冷媒温度制御下限値(第二閾値)、bは吐出冷媒温度制御上限値(第一閾値)、cは圧縮機許容温度上限値を示す。
FIG. 5 is a graph showing changes in the discharged refrigerant temperature in refrigerators according to some embodiments of the present disclosure.
In FIG. 5, the vertical axis represents the temperature of refrigerant discharged from the compressor 52, and the horizontal axis represents time. Moreover, in discharge refrigerant temperature, d shows the discharge refrigerant temperature control lower limit (second threshold value) mentioned later, b shows discharge refrigerant temperature control upper limit (first threshold), and c shows compressor allowable temperature upper limit.

図5の時間0の時点では、蒸発器出口過熱度制御が行われている。時間0から時間が経過すると、圧縮機2の吐出冷媒温度は上昇し、時間t7において吐出冷媒温度制御上限値bに到達する。吐出冷媒温度が吐出冷媒温度制御上限値bに到達すると、蒸発器出口過熱度制御を停止し、吐出冷媒温度保護制御が開始される。   At time 0 in FIG. 5, the evaporator outlet superheat degree control is performed. When time elapses from time 0, the discharge refrigerant temperature of the compressor 2 rises and reaches the discharge refrigerant temperature control upper limit b at time t7. When the discharge refrigerant temperature reaches the discharge refrigerant temperature control upper limit b, the evaporator outlet superheat degree control is stopped and the discharge refrigerant temperature protection control is started.

前述したように、吐出冷媒温度保護制御は、吐出冷媒温度を第二所定範囲の値に制御するものである。吐出冷媒温度センサ7が計測する吐出冷媒温度を吐出冷媒温度制御下限値(第二閾値)dから吐出冷媒温度制御上限値(第一閾値)bの範囲である第二所定範囲の値となるように、制御装置10が膨張弁5の開度を制御する。   As described above, the discharged refrigerant temperature protection control controls the discharged refrigerant temperature to a value within the second predetermined range. The discharge refrigerant temperature measured by the discharge refrigerant temperature sensor 7 is set to a value within a second predetermined range that is a range from the discharge refrigerant temperature control lower limit (second threshold) d to the discharge refrigerant temperature control upper limit (first threshold) b. Furthermore, the control device 10 controls the opening degree of the expansion valve 5.

時間t7において吐出冷媒温度保護制御が開始されると、膨張弁5の開度が開方向に制御される。膨張弁5の開度が開方向に制御されてから圧縮機2の吐出冷媒温度が下がり始めるにはタイムラグがあるため、時間t7を過ぎて一定時間経過後、吐出冷媒温度は下がり始める。
吐出冷媒温度保護制御にて、図2のフローチャートに示される制御が行われることにより、圧縮機2の吐出冷媒温度は、大きな変動が抑えられ、第二所定範囲内で推移するように制御される。そのため、本開示の幾つかの実施形態によれば、安定した運転が継続可能である。
When the discharged refrigerant temperature protection control is started at time t7, the opening degree of the expansion valve 5 is controlled in the opening direction. Since there is a time lag when the discharge refrigerant temperature of the compressor 2 starts to decrease after the opening degree of the expansion valve 5 is controlled in the opening direction, the discharge refrigerant temperature starts to decrease after a lapse of a certain time after the time t7.
By performing the control shown in the flowchart of FIG. 2 in the discharge refrigerant temperature protection control, the discharge refrigerant temperature of the compressor 2 is controlled such that a large fluctuation is suppressed and the temperature changes within the second predetermined range. . Therefore, according to some embodiments of the present disclosure, stable operation can be continued.

また、参考例としての冷凍機においては、液バイパス制御が頻繁にオンオフされることを避けるため、液バイパス制御終了温度aと吐出冷媒温度制御上限値bとの差が大きくされている。一方、本開示の幾つかの実施形態に係る冷凍機においては、膨張弁5で細かく冷媒流量を制御できる。そのため、吐出冷媒温度を圧縮機許容温度上限値以下に維持するのに必要な最小液戻し量に制御が可能である。これにより、吐出冷媒温度制御下限値dと吐出冷媒温度制御上限値bとの差を小さくすることができる。吐出冷媒温度の高低は、冷凍機の能力の高低と比例することから、吐出冷媒温度を高い値で推移させることは、冷凍機の能力も高い値で推移させることとなる。   Further, in the refrigerator as a reference example, the difference between the liquid bypass control end temperature a and the discharge refrigerant temperature control upper limit b is increased in order to avoid frequent switching of the liquid bypass control. On the other hand, in the refrigerator according to some embodiments of the present disclosure, the refrigerant flow rate can be finely controlled by the expansion valve 5. Therefore, it is possible to control to the minimum liquid return amount necessary to maintain the discharged refrigerant temperature below the compressor allowable temperature upper limit value. Thereby, the difference between the discharged refrigerant temperature control lower limit d and the discharged refrigerant temperature control upper limit b can be reduced. Since the level of the discharged refrigerant temperature is proportional to the level of the capacity of the refrigerator, changing the discharged refrigerant temperature at a high value also changes the capacity of the refrigerator at a high value.

図6は、参考例としての冷凍機における冷凍能力の変化を示したグラフである。
図6において、縦軸は冷凍機の冷凍能力、横軸は凝縮器の吸込空気温度である。凝縮器の吸込空気温度は、すなわち外気温にほぼ等しい。また、冷凍能力において、R1は吸込空気温度T1で蒸発器出口過熱度制御から吐出冷媒温度保護制御(この場合、液バイパス制御)に切り替わった場合の冷凍能力、R2は、吸込空気温度T2の場合の冷凍能力を示す。また、実線が冷凍能力と凝縮器の吸込空気温度との関係を示しており、一点鎖線は、通常の蒸発器出口過熱度制御を行った場合に想定される冷凍能力の推移を示す。
FIG. 6 is a graph showing changes in the refrigeration capacity in a refrigerator as a reference example.
In FIG. 6, the vertical axis represents the refrigeration capacity of the refrigerator, and the horizontal axis represents the intake air temperature of the condenser. The intake air temperature of the condenser is approximately equal to the outside air temperature. In the refrigerating capacity, R1 is the refrigerating capacity when switching from the evaporator outlet superheat degree control to the discharge refrigerant temperature protection control (in this case, liquid bypass control) at the suction air temperature T1, and R2 is the suction air temperature T2. Shows the refrigerating capacity. The solid line indicates the relationship between the refrigerating capacity and the intake air temperature of the condenser, and the alternate long and short dash line indicates the transition of the refrigerating capacity that is assumed when normal evaporator outlet superheat control is performed.

参考例としての冷凍機においては、吸込空気温度T1で液バイパス制御が開始された場合の冷凍能力R1と比較して、吸込空気温度が上がり、吸込空気温度T2となった場合の冷凍能力R2は、大きく冷凍能力が低下している。すなわち、吸込空気温度が高い場合は、常に吐出冷媒温度保護制御を行わねばならず、液バイパスライン59を常に開とすることとなる。   In the refrigerator as a reference example, the refrigerating capacity R2 when the intake air temperature rises and becomes the intake air temperature T2 is compared with the refrigerating capacity R1 when the liquid bypass control is started at the intake air temperature T1. The refrigerating capacity is greatly reduced. That is, when the intake air temperature is high, the discharge refrigerant temperature protection control must always be performed, and the liquid bypass line 59 is always opened.

図7は、本開示の幾つかの実施形態に係る冷凍機における冷凍能力の変化を示したグラフである。
図7において、縦軸は冷凍機の冷凍能力、横軸は凝縮器の吸込空気温度である。また、冷凍能力において、R1は吸込空気温度T1で蒸発器出口過熱度制御から吐出冷媒温度保護制御に切り替わった場合の冷凍能力、R3は、吸込空気温度T2の場合の冷凍能力を示す。また、実線が冷凍能力と凝縮器の吸込空気温度との関係を示しており、一点鎖線は、通常の蒸発器出口過熱度制御を行った場合に想定される冷凍能力の推移を示す。
FIG. 7 is a graph showing changes in the refrigeration capacity in the refrigerator according to some embodiments of the present disclosure.
In FIG. 7, the vertical axis represents the refrigeration capacity of the refrigerator, and the horizontal axis represents the intake air temperature of the condenser. Further, in the refrigerating capacity, R1 indicates the refrigerating capacity when switching from the evaporator outlet superheat degree control to the discharge refrigerant temperature protection control at the intake air temperature T1, and R3 indicates the refrigerating capacity at the intake air temperature T2. The solid line indicates the relationship between the refrigerating capacity and the intake air temperature of the condenser, and the alternate long and short dash line indicates the transition of the refrigerating capacity that is assumed when normal evaporator outlet superheat control is performed.

本開示の幾つかの実施形態に係る冷凍機においては、吸込空気温度T1で吐出冷媒温度保護制御が開始された場合の冷凍能力R1と比較して、吸込空気温度が上がり、吸込空気温度T2となった場合の冷凍能力R3は低下しているが、冷凍能力の低下が少ない。これは、図5で示されたように、吐出冷媒温度の低下が少ないことに因る。ここで、R3はR2よりも大きい値である。   In the refrigerator according to some embodiments of the present disclosure, the intake air temperature is increased compared to the refrigerating capacity R1 when the discharge refrigerant temperature protection control is started at the intake air temperature T1, and the intake air temperature T2 In this case, the refrigeration capacity R3 is decreased, but the decrease in the refrigeration capacity is small. This is because, as shown in FIG. 5, the discharge refrigerant temperature decreases little. Here, R3 is a value larger than R2.

図8は、参考例としての冷凍機における圧力−エンタルピ線図である。
図8において、縦軸は圧力、横軸はエンタルピである。太実線は、蒸発器出口過熱度制御時の冷凍サイクルを示し、太破線は、その場合の等温度曲線を示す。また実線は、液バイパス制御時の冷凍サイクルを示し、破線は、その場合の等温度曲線を示す。また一点鎖線は、飽和曲線を示す。
FIG. 8 is a pressure-enthalpy diagram in a refrigerator as a reference example.
In FIG. 8, the vertical axis represents pressure and the horizontal axis represents enthalpy. A thick solid line shows the refrigerating cycle at the time of evaporator outlet superheat control, and a thick broken line shows the isothermal curve in that case. The solid line shows the refrigeration cycle during the liquid bypass control, and the broken line shows the isothermal curve in that case. Moreover, a dashed-dotted line shows a saturation curve.

参考例としての冷凍機における蒸発器出口過熱度制御時の図8に示される冷凍サイクルにおいて、h1は気液内部熱交換器54のガス冷媒の出口、h3は気液内部熱交換器54の液冷媒の入口、h4は気液内部熱交換器54の液冷媒の出口、h6は気液内部熱交換器54のガス冷媒の入口を示す。
また、液バイパス制御時の図8に示される冷凍サイクルにおいて、h1′は気液内部熱交換器54のガス冷媒の出口、h3′は気液内部熱交換器54の液冷媒の入口、h4′は気液内部熱交換器54の液冷媒の出口、h6′は気液内部熱交換器54のガス冷媒の入口を示す。
In the refrigerating cycle shown in FIG. 8 at the time of evaporator outlet superheat control in the refrigerator as a reference example, h1 is the outlet of the gas refrigerant of the gas-liquid internal heat exchanger 54, h3 is the liquid of the gas-liquid internal heat exchanger 54 The refrigerant inlet, h4 indicates the liquid refrigerant outlet of the gas-liquid internal heat exchanger 54, and h6 indicates the gas refrigerant inlet of the gas-liquid internal heat exchanger 54.
In the refrigeration cycle shown in FIG. 8 at the time of liquid bypass control, h1 ′ is the gas refrigerant outlet of the gas-liquid internal heat exchanger 54, h3 ′ is the liquid refrigerant inlet of the gas-liquid internal heat exchanger 54, h4 ′. Is the liquid refrigerant outlet of the gas-liquid internal heat exchanger 54, and h6 'is the gas refrigerant inlet of the gas-liquid internal heat exchanger 54.

また図9は、本開示の幾つかの実施形態に係る冷凍機における圧力−エンタルピ線図である。
図9において、縦軸は圧力、横軸はエンタルピである。太実線は、蒸発器出口過熱度制御時の冷凍サイクルを示し、太破線は、その場合の等温度曲線を示す。また実線は、吐出冷媒温度保護制御時の冷凍サイクルを示し、破線は、その場合の等温度曲線を示す。また一点鎖線は、飽和曲線を示す。
FIG. 9 is a pressure-enthalpy diagram in a refrigerator according to some embodiments of the present disclosure.
In FIG. 9, the vertical axis represents pressure, and the horizontal axis represents enthalpy. A thick solid line shows the refrigerating cycle at the time of evaporator outlet superheat control, and a thick broken line shows the isothermal curve in that case. A solid line indicates a refrigeration cycle during discharge refrigerant temperature protection control, and a broken line indicates an isothermal curve in that case. Moreover, a dashed-dotted line shows a saturation curve.

本開示の幾つかの実施形態に係る冷凍機における蒸発器出口過熱度制御時の図9に示される冷凍サイクルにおいて、h1は気液内部熱交換器54のガス冷媒の出口、h3は気液内部熱交換器54の液冷媒の入口、h4は気液内部熱交換器54の液冷媒の出口、h6は気液内部熱交換器54のガス冷媒の入口を示す。
また、液バイパス制御時の図9に示される冷凍サイクルにおいて、h1″は気液内部熱交換器54のガス冷媒の出口、h3″は気液内部熱交換器54の液冷媒の入口、h4″は気液内部熱交換器54の液冷媒の出口、h6″は気液内部熱交換器54のガス冷媒の入口を示す。
In the refrigeration cycle shown in FIG. 9 at the time of evaporator outlet superheat control in a refrigerator according to some embodiments of the present disclosure, h1 is the gas refrigerant outlet of the gas-liquid internal heat exchanger 54, and h3 is the gas-liquid internal The liquid refrigerant inlet of the heat exchanger 54, h4 is the liquid refrigerant outlet of the gas-liquid internal heat exchanger 54, and h6 is the gas refrigerant inlet of the gas-liquid internal heat exchanger 54.
In the refrigeration cycle shown in FIG. 9 at the time of liquid bypass control, h1 ″ is the gas refrigerant outlet of the gas-liquid internal heat exchanger 54, h3 ″ is the liquid refrigerant inlet of the gas-liquid internal heat exchanger 54, and h4 ″. Is the liquid refrigerant outlet of the gas-liquid internal heat exchanger 54, and h6 ″ is the gas refrigerant inlet of the gas-liquid internal heat exchanger 54.

参考例としての冷凍機において、通常の蒸発器出口過熱度制御から液バイパス制御に制御を切替えると、吐出冷媒温度の低下、及び冷凍能力の低下が起こる。
また本開示の幾つかの実施形態に係る冷凍機において、通常の蒸発器出口過熱度制御から吐出冷媒温度保護制御に制御を切替えると、同様に吐出冷媒温度の低下、及び冷凍能力の低下が起こる。
In the refrigerator as a reference example, when the control is switched from the normal evaporator outlet superheat degree control to the liquid bypass control, the discharge refrigerant temperature and the refrigeration capacity decrease.
Further, in the refrigerator according to some embodiments of the present disclosure, when the control is switched from the normal evaporator outlet superheat degree control to the discharge refrigerant temperature protection control, the discharge refrigerant temperature and the refrigerating capacity are similarly reduced. .

参考例としての冷凍機において、通常の蒸発器出口過熱度制御から液バイパス制御に制御を切替えると、蒸発器出口過熱度制御における吐出冷媒温度を示す等温度曲線(太破線)が、液バイパス制御における吐出冷媒温度を示す等温度曲線(破線)に移動し、この移動距離が吐出冷媒温度の温度差として表れる。   In a refrigerator as a reference example, when the control is switched from normal evaporator outlet superheat control to liquid bypass control, an isothermal curve (thick broken line) indicating the discharge refrigerant temperature in the evaporator outlet superheat control is liquid bypass control. It moves to the isothermal curve (broken line) which shows the discharge refrigerant temperature in this, and this movement distance appears as a temperature difference of discharge refrigerant temperature.

一方、本開示の幾つかの実施形態に係る冷凍機において、通常の蒸発器出口過熱度制御から吐出冷媒温度保護制御に制御を切替えると、蒸発器出口過熱度制御における吐出冷媒温度を示す等温度曲線(太破線)が、吐出冷媒温度保護制御における吐出冷媒温度を示す等温度曲線(破線)に移動し、この移動距離が吐出冷媒温度の温度差として表れる。
このように、本開示の幾つかの実施形態に係る冷凍機によれば、圧縮機2の吐出冷媒温度は、圧縮機許容温度上限値以下に維持するのに必要な温度低下にとどめることができる。
よって、液バイパス制御と比較して、吐出冷媒温度の低下を抑えることができる。
On the other hand, in the refrigerators according to some embodiments of the present disclosure, when the control is switched from normal evaporator outlet superheat control to discharged refrigerant temperature protection control, an equal temperature indicating the discharged refrigerant temperature in the evaporator outlet superheat control. The curve (thick broken line) moves to an isothermal curve (broken line) indicating the discharged refrigerant temperature in the discharged refrigerant temperature protection control, and this moving distance appears as a temperature difference between the discharged refrigerant temperatures.
As described above, according to the refrigerators according to some embodiments of the present disclosure, the discharge refrigerant temperature of the compressor 2 can be limited to the temperature decrease necessary to maintain the compressor allowable temperature upper limit value or less. .
Therefore, compared with liquid bypass control, the fall of discharge refrigerant temperature can be suppressed.

また、参考例としての冷凍機において、通常の蒸発器出口過熱度制御から液バイパス制御に制御を切替えると、冷媒の蒸発温度はh1からh1′へ、またはh6からh6′へ、その差x′だけ上昇する。よって、差x′に相当する冷凍能力が低下する。
また、液バイパス制御が行われると、h3′からh1′へ液冷媒がバイパスされるため、h3′とh1′との差y(二点鎖線部分)に相当する冷凍能力が低下する。
以上より、参考例としての冷凍機においては、x′+yに相当する冷凍能力が低下する。
Further, in the refrigerator as the reference example, when the control is switched from the normal evaporator outlet superheat degree control to the liquid bypass control, the refrigerant evaporating temperature is changed from h1 to h1 'or from h6 to h6', the difference x ' Only rise. Therefore, the refrigerating capacity corresponding to the difference x ′ decreases.
Further, when the liquid bypass control is performed, the liquid refrigerant is bypassed from h3 ′ to h1 ′, so that the refrigerating capacity corresponding to the difference y (the two-dot chain line portion) between h3 ′ and h1 ′ is lowered.
From the above, in the refrigerator as a reference example, the refrigeration capacity corresponding to x ′ + y is lowered.

一方、本開示の幾つかの実施形態に係る冷凍機において、通常の蒸発器出口過熱度制御から吐出冷媒温度保護制御に制御を切替えると、冷媒の蒸発温度はh1からh1″へ、またはh6からh6″へ、その差x″だけ上昇する。よって、差x″に相当する冷凍能力が低下する。
このように、本開示の幾つかの実施形態に係る冷凍機の冷凍能力の低下は、液バイパス制御時の能力の低下と比較して少ない。よって、本開示の幾つかの実施形態に係る冷凍機によれば、冷凍能力の低下を小さく抑えることができる。
On the other hand, in the refrigerator according to some embodiments of the present disclosure, when the control is switched from normal evaporator outlet superheat control to discharged refrigerant temperature protection control, the refrigerant evaporation temperature is changed from h1 to h1 ″ or from h6. The difference x ″ increases to h6 ″. Therefore, the refrigerating capacity corresponding to the difference x ″ decreases.
As described above, the decrease in the refrigerating capacity of the refrigerators according to some embodiments of the present disclosure is less than the decrease in the capacity during the liquid bypass control. Therefore, according to the refrigerator according to some embodiments of the present disclosure, it is possible to suppress a decrease in the refrigerating capacity.

以上、説明してきたように、本実施形態に係る冷凍機の制御装置、冷凍機、冷凍機の制御方法および冷凍機の制御プログラムによれば、以下の作用効果を奏する。
本開示によれば、吐出冷媒温度が吐出冷媒温度制御上限値以下に制御されるため、圧縮機2がほぼ停止することなく連続した運転が可能である。
また、蒸発器6に余剰に供給された冷媒の冷媒熱エネルギーが気液内部熱交換器4で回収されるため、冷凍能力の低下を極めて小さく抑えることができる。
また、圧縮機2が冷媒ガス吸入を維持できるため、液冷媒が吸入されず油が希釈しないことから、圧縮機2の潤滑性に影響が及ぶことがない。
また、膨張弁5で冷媒流量を細かく制御できることから、吐出冷媒温度を吐出冷媒温度制御上限値以下に維持するのに必要な最小液戻し量に制御が可能であり、安定した運転が可能である。
As described above, according to the refrigerator control device, the refrigerator, the refrigerator control method, and the refrigerator control program according to the present embodiment, the following operational effects can be obtained.
According to the present disclosure, since the discharge refrigerant temperature is controlled to be equal to or lower than the discharge refrigerant temperature control upper limit value, the compressor 2 can be continuously operated without substantially stopping.
Moreover, since the refrigerant | coolant thermal energy of the refrigerant | coolant supplied to the evaporator 6 excessively is collect | recovered by the gas-liquid internal heat exchanger 4, the fall of refrigerating capacity can be suppressed very small.
Further, since the compressor 2 can maintain the refrigerant gas suction, the liquid refrigerant is not sucked and the oil is not diluted, so that the lubricity of the compressor 2 is not affected.
Further, since the refrigerant flow rate can be finely controlled by the expansion valve 5, it is possible to control to the minimum liquid return amount necessary to maintain the discharge refrigerant temperature below the upper limit value of the discharge refrigerant temperature control, and stable operation is possible. .

さらに、圧縮機2の吐出冷媒温度が吐出冷媒温度制御上限値bよりも小さい吐出冷媒温度制御下限値dを下回る値であり、かつ蒸発器6出口の冷媒過熱度が冷媒過熱度制御下限値以上の場合は、吐出冷媒温度保護制御を停止し、蒸発器出口過熱度制御によって膨張弁5の開度を制御する。蒸発器6出口の冷媒過熱度が確保されているのを確認した上で、吐出冷媒温度保護制御を終了して通常の蒸発器出口過熱度制御に移行させ、吐出冷媒温度保護制御によって下がりすぎた圧縮機2の吐出冷媒温度を上げることができる。   Further, the discharge refrigerant temperature of the compressor 2 is a value lower than the discharge refrigerant temperature control lower limit value d smaller than the discharge refrigerant temperature control upper limit value b, and the refrigerant superheat degree at the outlet of the evaporator 6 is equal to or higher than the refrigerant superheat degree control lower limit value. In this case, the discharge refrigerant temperature protection control is stopped, and the opening degree of the expansion valve 5 is controlled by the evaporator outlet superheat degree control. After confirming that the refrigerant superheat degree at the outlet of the evaporator 6 is secured, the discharge refrigerant temperature protection control is finished and the routine is shifted to the normal evaporator outlet superheat degree control. The refrigerant temperature discharged from the compressor 2 can be raised.

また本開示によれば、圧縮機2の吐出冷媒温度が吐出冷媒温度制御下限値dを下回る値であり、かつ、蒸発器6出口の冷媒過熱度が冷媒過熱度制御下限値を下回る値である場合は、吐出冷媒温度保護制御を停止し、蒸発器出口過熱度制御によって膨張弁5の開度を閉方向に制御する。吐出冷媒温度保護制御によって圧縮機2の吐出冷媒温度が下がっているとともに、蒸発器6出口の冷媒過熱度が確保すべき値の下限値を下回ることで圧縮機2に液バックが生じる可能性がある。しかし本開示によれば、膨張弁5の開度を閉方向に制御するため、蒸発器6出口の冷媒過熱度を高めることができる。さらに、圧縮機2の吐出冷媒温度を上げることができる。   Further, according to the present disclosure, the discharge refrigerant temperature of the compressor 2 is a value lower than the discharge refrigerant temperature control lower limit value d, and the refrigerant superheat degree at the outlet of the evaporator 6 is lower than the refrigerant superheat degree control lower limit value. In this case, the discharge refrigerant temperature protection control is stopped, and the opening degree of the expansion valve 5 is controlled in the closing direction by the evaporator outlet superheat degree control. The discharge refrigerant temperature of the compressor 2 is lowered by the discharge refrigerant temperature protection control, and a liquid back may occur in the compressor 2 when the refrigerant superheat degree at the outlet of the evaporator 6 falls below the lower limit value to be ensured. is there. However, according to the present disclosure, the degree of refrigerant superheating at the outlet of the evaporator 6 can be increased because the opening degree of the expansion valve 5 is controlled in the closing direction. Furthermore, the discharge refrigerant temperature of the compressor 2 can be raised.

また本開示によれば、圧縮機2の吐出冷媒温度が吐出冷媒温度制御下限値d以上、かつ吐出冷媒温度制御上限値b以下の値である場合は、吐出冷媒温度保護制御による膨張弁5の開度を保持するように制御する。これにより、吐出冷媒温度保護制御において、圧縮機2の吐出冷媒温度を吐出冷媒温度制御下限値d以上、かつ吐出冷媒温度制御上限値b以下の第二所定範囲内となるように制御するため、吐出冷媒温度の変動が少なく、安定した運転を継続可能である。また、冷凍機の能力を確保し維持することができる。   Further, according to the present disclosure, when the discharge refrigerant temperature of the compressor 2 is not less than the discharge refrigerant temperature control lower limit value d and not more than the discharge refrigerant temperature control upper limit value b, the expansion valve 5 is controlled by the discharge refrigerant temperature protection control. Control to maintain the opening. Thereby, in the discharge refrigerant temperature protection control, in order to control the discharge refrigerant temperature of the compressor 2 to be within the second predetermined range of the discharge refrigerant temperature control lower limit d or more and the discharge refrigerant temperature control upper limit b or less, There is little fluctuation in the discharged refrigerant temperature, and stable operation can be continued. In addition, the capacity of the refrigerator can be secured and maintained.

また本開示によれば、吐出冷媒温度保護制御によって膨張弁5の開度を制御してから所定時間以上経過した場合、圧縮機2の吐出冷媒温度が吐出冷媒温度制御上限値bを超えたか否かの判定を行う。これにより、所定時間経過し、冷凍機の冷媒回路が定常状態になってから圧縮機2の吐出冷媒温度の判定を行うため、正しく判定を行うことができる。   Further, according to the present disclosure, whether or not the discharge refrigerant temperature of the compressor 2 has exceeded the discharge refrigerant temperature control upper limit b when a predetermined time or more has elapsed since the opening of the expansion valve 5 was controlled by the discharge refrigerant temperature protection control. Judgment is made. Thus, since the refrigerant temperature discharged from the compressor 2 is determined after a predetermined time has elapsed and the refrigerant circuit of the refrigerator has reached a steady state, the determination can be made correctly.

また本開示によれば、冷媒過熱度制御下限値は、蒸発器出口過熱度制御における目標冷媒過熱度よりも小さい値であることから、蒸発器6出口の冷媒過熱度を最低限確保し、圧縮機2の液バックの発生を抑制することができる。   Further, according to the present disclosure, the refrigerant superheat degree control lower limit value is a value smaller than the target refrigerant superheat degree in the evaporator outlet superheat degree control. The occurrence of liquid back in the machine 2 can be suppressed.

1、51 冷凍サイクル
2、52 圧縮機
3、53 凝縮器
4、54 気液内部熱交換器(熱交換器)
5、55 膨張弁
6、56 蒸発器
7、57 吐出冷媒温度センサ
8、58 冷媒配管
10、50 制御装置
59 液バイパスライン
1, 51 Refrigeration cycle 2, 52 Compressor 3, 53 Condenser 4, 54 Gas-liquid internal heat exchanger (heat exchanger)
5, 55 Expansion valve 6, 56 Evaporator 7, 57 Discharge refrigerant temperature sensor 8, 58 Refrigerant piping 10, 50 Control device 59 Liquid bypass line

Claims (8)

冷媒を圧縮する圧縮機と、
該圧縮機により圧縮された冷媒を凝縮する凝縮器と、
該凝縮器から導かれた液冷媒を膨張させるとともに、蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、
該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御装置であって、
前記圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御し、
前記圧縮機の前記吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御する冷凍機の制御装置。
A compressor for compressing the refrigerant;
A condenser for condensing the refrigerant compressed by the compressor;
An expansion valve whose opening is controlled by an evaporator outlet superheat degree control that expands the liquid refrigerant guided from the condenser and controls the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range;
The evaporator for evaporating the refrigerant led from the expansion valve, and a control device for a refrigerator comprising:
When the discharge refrigerant temperature of the compressor exceeds the first threshold, the evaporator outlet superheat degree control is stopped, and the expansion is performed by discharge refrigerant temperature protection control for controlling the discharge refrigerant temperature to a value within a second predetermined range. Control the opening of the valve in the opening direction,
When the discharge refrigerant temperature of the compressor is lower than a second threshold value that is smaller than a first threshold value, and the refrigerant superheat degree at the outlet of the evaporator is equal to or greater than a third threshold value, the discharge refrigerant temperature protection The control apparatus of the refrigerator which stops control and controls the opening degree of the said expansion valve by the said evaporator exit superheat degree control.
前記圧縮機の前記吐出冷媒温度が前記第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が前記第三閾値を下回る値である場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を閉方向に制御する請求項1に記載の冷凍機の制御装置。   When the discharge refrigerant temperature of the compressor is lower than the second threshold value and the refrigerant superheat degree at the outlet of the evaporator is lower than the third threshold value, the discharge refrigerant temperature protection control The refrigerator control device according to claim 1, wherein the opening degree of the expansion valve is controlled in the closing direction by controlling the degree of superheat of the evaporator outlet. 前記圧縮機の前記吐出冷媒温度が前記第二閾値以上、かつ前記第一閾値以下の値である場合は、前記吐出冷媒温度保護制御による前記膨張弁の開度を保持するように制御する請求項1または請求項2に記載の冷凍機の制御装置。   The control is performed to maintain the opening degree of the expansion valve by the discharge refrigerant temperature protection control when the discharge refrigerant temperature of the compressor is not less than the second threshold and not more than the first threshold. The control apparatus of the refrigerator of Claim 1 or Claim 2. 前記吐出冷媒温度保護制御によって前記膨張弁の開度を制御してから所定時間以上経過した場合、前記圧縮機の前記吐出冷媒温度が前記第一閾値を超えたか否かの判定を行う請求項1から請求項3のいずれかに記載の冷凍機の制御装置。   2. A determination is made as to whether or not the discharge refrigerant temperature of the compressor has exceeded the first threshold when a predetermined time or more has elapsed since the opening of the expansion valve was controlled by the discharge refrigerant temperature protection control. The control apparatus of the refrigerator in any one of Claim 3. 前記第三閾値は、前記蒸発器出口過熱度制御における目標冷媒過熱度よりも小さい値である請求項1から請求項4のいずれかに記載の冷凍機の制御装置。   The control apparatus for a refrigerator according to any one of claims 1 to 4, wherein the third threshold value is a value smaller than a target refrigerant superheat degree in the evaporator outlet superheat degree control. 冷媒を圧縮する圧縮機と、
該圧縮機により圧縮された冷媒を凝縮する凝縮器と、
該凝縮器から導かれた液冷媒を膨張させるとともに、蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、
該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、
請求項1から請求項5のいずれかに記載の制御装置と、を備える冷凍機。
A compressor for compressing the refrigerant;
A condenser for condensing the refrigerant compressed by the compressor;
An expansion valve whose opening is controlled by an evaporator outlet superheat degree control that expands the liquid refrigerant guided from the condenser and controls the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range;
The evaporator for evaporating the refrigerant guided from the expansion valve;
A refrigerator comprising: the control device according to any one of claims 1 to 5.
冷媒を圧縮する圧縮機と、
該圧縮機により圧縮された冷媒を凝縮する凝縮器と、
該凝縮器から導かれた液冷媒を膨張させるとともに、蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、
該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御方法であって、
前記圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御する工程と、
前記圧縮機の前記吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御する工程と、を有する冷凍機の制御方法。
A compressor for compressing the refrigerant;
A condenser for condensing the refrigerant compressed by the compressor;
An expansion valve whose opening is controlled by an evaporator outlet superheat degree control that expands the liquid refrigerant guided from the condenser and controls the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range;
A method of controlling a refrigerator comprising: the evaporator that evaporates the refrigerant guided from the expansion valve;
When the discharge refrigerant temperature of the compressor exceeds the first threshold, the evaporator outlet superheat degree control is stopped, and the expansion is performed by discharge refrigerant temperature protection control for controlling the discharge refrigerant temperature to a value within a second predetermined range. Controlling the opening of the valve in the opening direction;
When the discharge refrigerant temperature of the compressor is lower than a second threshold value that is smaller than a first threshold value, and the refrigerant superheat degree at the outlet of the evaporator is equal to or greater than a third threshold value, the discharge refrigerant temperature protection And a step of controlling the opening degree of the expansion valve by controlling the degree of superheat of the evaporator outlet.
冷媒を圧縮する圧縮機と、
該圧縮機により圧縮された冷媒を凝縮する凝縮器と、
該凝縮器から導かれた液冷媒を膨張させるとともに、蒸発器の出口の冷媒過熱度を第一所定範囲の値に制御する蒸発器出口過熱度制御によって開度が制御される膨張弁と、
該膨張弁から導かれた冷媒を蒸発させる前記蒸発器と、を備えた冷凍機の制御プログラムであって、
前記圧縮機の吐出冷媒温度が第一閾値を超えた場合は、前記蒸発器出口過熱度制御を停止し、前記吐出冷媒温度を第二所定範囲の値に制御する吐出冷媒温度保護制御によって前記膨張弁の開度を開方向に制御するステップと、
前記圧縮機の前記吐出冷媒温度が第一閾値よりも小さい第二閾値を下回る値であり、かつ、前記蒸発器の出口の前記冷媒過熱度が第三閾値以上の場合は、前記吐出冷媒温度保護制御を停止し、前記蒸発器出口過熱度制御によって前記膨張弁の開度を制御するステップと、を有する冷凍機の制御プログラム。

A compressor for compressing the refrigerant;
A condenser for condensing the refrigerant compressed by the compressor;
An expansion valve whose opening is controlled by an evaporator outlet superheat degree control that expands the liquid refrigerant guided from the condenser and controls the refrigerant superheat degree at the outlet of the evaporator to a value within a first predetermined range;
A control program for a refrigerator comprising the evaporator for evaporating the refrigerant guided from the expansion valve,
When the discharge refrigerant temperature of the compressor exceeds the first threshold, the evaporator outlet superheat degree control is stopped, and the expansion is performed by discharge refrigerant temperature protection control for controlling the discharge refrigerant temperature to a value within a second predetermined range. Controlling the opening of the valve in the opening direction;
When the discharge refrigerant temperature of the compressor is lower than a second threshold value that is smaller than a first threshold value, and the refrigerant superheat degree at the outlet of the evaporator is equal to or greater than a third threshold value, the discharge refrigerant temperature protection A control program for the refrigerator, comprising: stopping control and controlling the opening degree of the expansion valve by the evaporator outlet superheat degree control.

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