[go: up one dir, main page]

JP5447499B2 - Refrigeration equipment - Google Patents

Refrigeration equipment Download PDF

Info

Publication number
JP5447499B2
JP5447499B2 JP2011290079A JP2011290079A JP5447499B2 JP 5447499 B2 JP5447499 B2 JP 5447499B2 JP 2011290079 A JP2011290079 A JP 2011290079A JP 2011290079 A JP2011290079 A JP 2011290079A JP 5447499 B2 JP5447499 B2 JP 5447499B2
Authority
JP
Japan
Prior art keywords
refrigerant
heat exchanger
indoor
target value
detector
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2011290079A
Other languages
Japanese (ja)
Other versions
JP2013139924A (en
Inventor
忠史 西村
智 石田
伸樹 松井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daikin Industries Ltd
Original Assignee
Daikin Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to JP2011290079A priority Critical patent/JP5447499B2/en
Application filed by Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to CN201280064456.3A priority patent/CN104024764B/en
Priority to US14/368,704 priority patent/US20140373564A1/en
Priority to KR1020147020685A priority patent/KR101479458B1/en
Priority to BR112014015866A priority patent/BR112014015866A8/en
Priority to PCT/JP2012/083565 priority patent/WO2013099898A1/en
Priority to ES12862685T priority patent/ES2861271T3/en
Priority to AU2012361734A priority patent/AU2012361734B2/en
Priority to EP12862685.0A priority patent/EP2806233B1/en
Publication of JP2013139924A publication Critical patent/JP2013139924A/en
Application granted granted Critical
Publication of JP5447499B2 publication Critical patent/JP5447499B2/en
Priority to AU2016202855A priority patent/AU2016202855B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • 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
    • F25B39/00Evaporators; Condensers
    • F25B39/02Evaporators
    • F25B39/028Evaporators having distributing means
    • 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
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/005Compression machines, plants or systems with non-reversible cycle of the single unit type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B49/00Arrangement or mounting of control or safety devices
    • F25B49/02Arrangement or mounting of control or safety devices for compression type machines, plants or systems
    • F25B49/022Compressor control arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B13/00Compression machines, plants or systems, with reversible cycle
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2313/00Compression machines, plants or systems with reversible cycle not otherwise provided for
    • F25B2313/023Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units
    • F25B2313/0233Compression machines, plants or systems with reversible cycle not otherwise provided for using multiple indoor units in parallel arrangements
    • 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
    • F25B2600/027Compressor control by controlling 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
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2509Economiser valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/25Control of valves
    • F25B2600/2513Expansion valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/19Pressures
    • F25B2700/193Pressures of the compressor
    • F25B2700/1933Suction pressures
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2104Temperatures of an indoor room or compartment
    • 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
    • F25B2700/2116Temperatures of a condenser
    • F25B2700/21163Temperatures of a condenser of the refrigerant at the outlet of 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
    • F25B2700/00Sensing or detecting of parameters; Sensors therefor
    • F25B2700/21Temperatures
    • F25B2700/2117Temperatures of an evaporator
    • F25B2700/21174Temperatures of an evaporator of the refrigerant at the inlet of 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
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Air Conditioning Control Device (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)

Description

本発明は、冷凍装置、特に蒸発器を含む冷凍回路を有する冷凍装置に関する。   The present invention relates to a refrigeration apparatus, and more particularly to a refrigeration apparatus having a refrigeration circuit including an evaporator.

従来から、冷媒を循環させる冷凍回路を備え、冷凍回路の室内熱交換器と室外熱交換器との間で熱を移送する冷凍装置が適用された空気調和装置が知られている。このような空気調和装置において、室内熱交換器や室外熱交換器で適切な熱交換を行わせるため、例えば特許文献1(特開2004−271066号公報)に記載されているように、蒸発器の出口の冷媒の過熱度を制御する過熱度制御が行われている。   2. Description of the Related Art Conventionally, there is known an air conditioner to which a refrigeration apparatus that includes a refrigeration circuit that circulates a refrigerant and that transfers heat between an indoor heat exchanger and an outdoor heat exchanger of the refrigeration circuit is applied. In such an air conditioner, in order to perform appropriate heat exchange with an indoor heat exchanger or an outdoor heat exchanger, for example, as described in Patent Document 1 (Japanese Patent Application Laid-Open No. 2004-27066), an evaporator The degree of superheat is controlled to control the degree of superheat of the refrigerant at the outlet.

ところで、近年、空気調和装置についても消費電力を抑制する省エネルギーに対する要求が高まっている。例えば、そのための対策の一つとして、冷凍サイクルにおける高圧と低圧の差が小さい低差圧にすることがある。このような空気調和装置において、冷媒充填量が多くかつ外気温が低い場合に蒸発温度を上げる運転を行うと、蒸発器として機能している室内熱交換器の手前で冷媒が過冷却状態となることがある。このように室内熱交換器において過冷却状態が発生すると、室内熱交換器の過熱度制御ができなくなるという問題が生じる。   By the way, in recent years, there is an increasing demand for energy saving that suppresses power consumption of air conditioners. For example, as one of measures for that purpose, there is a low differential pressure where the difference between the high pressure and the low pressure in the refrigeration cycle is small. In such an air conditioner, when the operation of raising the evaporation temperature is performed when the refrigerant charging amount is large and the outside air temperature is low, the refrigerant is supercooled in front of the indoor heat exchanger functioning as an evaporator. Sometimes. Thus, when a supercooled state occurs in the indoor heat exchanger, there arises a problem that the degree of superheat of the indoor heat exchanger cannot be controlled.

本発明の課題は、蒸発器の手前で冷媒が過冷却状態になり易い冷凍装置の過熱度制御を適切に行わせることである。   An object of the present invention is to appropriately perform superheat degree control of a refrigeration apparatus in which a refrigerant is likely to be in a supercooled state before an evaporator.

本発明の第1観点に係る冷凍装置は、圧縮機と放熱器と蒸発器とが順に接続されて冷媒が循環する冷媒回路が形成されている冷凍装置であって、蒸発器の流入側に設けられ、冷媒回路の高圧目標値、冷媒回路の低圧目標値及び蒸発器の流出側の過熱度目標値のうちの少なくとも一つに基づいて蒸発器に流入する冷媒の膨張を制御するための膨張機構と、蒸発器の流入側の冷媒の過冷却状態を検出するための検出器と、検出器の検出結果に基づいて蒸発器の流入側の冷媒が過冷却状態にあると判断した場合に、高圧目標値を上げる設定変更、低圧目標値を下げる設定変更及び過熱度目標値を上げる設定変更のうちの少なくとも一つの所定の設定変更を行い得る制御部と、を備える。 A refrigeration apparatus according to a first aspect of the present invention is a refrigeration apparatus in which a compressor, a radiator, and an evaporator are connected in order to form a refrigerant circuit in which refrigerant circulates, and is provided on the inflow side of the evaporator. Expansion mechanism for controlling expansion of the refrigerant flowing into the evaporator based on at least one of the high pressure target value of the refrigerant circuit, the low pressure target value of the refrigerant circuit, and the superheat degree target value on the outflow side of the evaporator And a detector for detecting the supercooled state of the refrigerant on the inflow side of the evaporator, and a high pressure when it is determined that the refrigerant on the inflow side of the evaporator is in the supercooled state based on the detection result of the detector. A control unit capable of performing at least one predetermined setting change among a setting change for raising the target value, a setting change for lowering the low pressure target value, and a setting change for raising the superheat degree target value.

第1観点に係る冷凍装置では、蒸発器の流入側の冷媒が過冷却状態にあると判断した場合に、高圧目標値を上げる、低圧目標値を下げる及び過熱度目標値を上げる設定変更のうちの少なくとも一つの設定変更を行って蒸発器の過熱度制御ができなくなる状況を回避できるので、蒸発器の過熱度の制御を適切に行なわせることができる。   In the refrigeration apparatus according to the first aspect, when it is determined that the refrigerant on the inflow side of the evaporator is in a supercooled state, among the setting changes that increase the high pressure target value, decrease the low pressure target value, and increase the superheat degree target value Since it is possible to avoid the situation where the superheat degree control of the evaporator cannot be performed by changing at least one of the above settings, it is possible to appropriately control the superheat degree of the evaporator.

本発明の第2観点に係る冷凍装置は、第1観点に係る冷凍装置において、制御部は、所定の設定変更を行なった後に、過冷却状態が解消したときには、所定の設定変更を元に戻すように構成されている。  In the refrigeration apparatus according to the second aspect of the present invention, in the refrigeration apparatus according to the first aspect, the control unit restores the predetermined setting change when the supercooling state is resolved after performing the predetermined setting change. It is configured as follows.

本発明の第3観点に係る冷凍装置は、第3観点に係る冷凍装置において、制御部は、所定の設定変更を行う場合の過冷却状態になったと判断するときの値と所定の設定変更を元に戻す場合の過冷却状態を脱したと判断するときの値との間に、ハンチング防止のためのマージンを設けている。  In the refrigeration apparatus according to the third aspect of the present invention, in the refrigeration apparatus according to the third aspect, the control unit changes the value and the predetermined setting change when it is determined that the supercooling state is reached when the predetermined setting change is performed. A margin for preventing hunting is provided between the value at which it is determined that the supercooled state has been removed when returning to the original state.

本発明の第観点に係る冷凍装置は、第1観点から第3観点のいずれかに係る冷凍装置において、蒸発器は、利用側熱交換器であり、制御部は、検出器の検出結果に基づいて利用側熱交換器の流入側の冷媒が過冷却状態にあると判断した場合に、低圧目標値を下げる設定変更及び過熱度目標値を上げる設定変更のうちの少なくとも一方を行い得る。 The refrigeration apparatus according to the fourth aspect of the present invention is the refrigeration apparatus according to any one of the first to third aspects, wherein the evaporator is a use-side heat exchanger, and the control unit uses the detection result of the detector. Based on this, when it is determined that the refrigerant on the inflow side of the use side heat exchanger is in a supercooled state, at least one of a setting change that lowers the low pressure target value and a setting change that increases the superheat degree target value can be performed.

観点に係る冷凍装置では、利用側熱交換器の流入側の冷媒が過冷却状態にあると判断した場合に、低圧目標値を下げる設定変更及び過熱度目標値を上げる設定変更のうちの少なくとも一方を行って過冷却状態を回避することができ、冷媒量が多いために、蒸発器として機能している利用側熱交換器の手前で冷媒が過冷却状態になり易い場合に十分な対応が可能になる。 In the refrigeration apparatus according to the fourth aspect , when it is determined that the refrigerant on the inflow side of the use-side heat exchanger is in the supercooled state, of the setting change that lowers the low pressure target value and the setting change that increases the superheat degree target value It is possible to avoid a supercooled state by performing at least one of them, and because the amount of refrigerant is large, it is sufficient when the refrigerant tends to be supercooled in front of the use side heat exchanger functioning as an evaporator Is possible.

本発明の第観点に係る冷凍装置は、第観点に係る冷凍装置において、検出器は、利用側熱交換器の流入側の圧力飽和温度を検出するための第1検出器と利用側熱交換器の流入側の冷媒の温度を検出するための第2検出器、又は第1検出器と膨張機構の流入側の冷媒の温度を検出するための第3検出器を含み、制御部は、第1検出器と第2検出器の検出結果の比較又は第1検出器と第3検出器の検出結果の比較に基づいて、利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かを判断し得る。 The refrigeration apparatus according to a fifth aspect of the present invention is the refrigeration apparatus according to the fourth aspect, wherein the detector is a first detector for detecting the pressure saturation temperature on the inflow side of the use side heat exchanger and the use side heat. A second detector for detecting the temperature of the refrigerant on the inflow side of the exchanger, or a third detector for detecting the temperature of the refrigerant on the inflow side of the expansion mechanism and the first detector, Whether the refrigerant on the inflow side of the use side heat exchanger is in a supercooled state based on the comparison of the detection results of the first detector and the second detector or the comparison of the detection results of the first detector and the third detector. It can be determined whether or not.

観点に係る冷凍装置では、利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かの判断を第1検出器と第2検出器の検出結果の比較又は第1検出器と第3検出器の検出結果の比較に基づいて行うので、利用側熱交換器の流入側の冷媒に過冷却がついていても、正確に過冷却状態の判断を行なうことができる。 In the refrigeration apparatus according to the fifth aspect, whether the refrigerant on the inflow side of the use side heat exchanger is in a supercooled state is determined by comparing the detection results of the first detector and the second detector or by the first detector. Therefore, even if the refrigerant on the inflow side of the use side heat exchanger is supercooled, it is possible to accurately determine the supercooled state.

本発明の第観点に係る冷凍装置は、第5観点の冷凍装置において、第3検出器は、放熱器の流出側に設けられている液管温度センサであり、制御部は、液管温度センサの取り付け位置から膨張機構までの熱損失に相当する補正値を液管温度センサの検出温度より差し引いて得られる温度を膨張機構の流入側の冷媒の温度として用いて利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かを判断し得る。 The refrigeration apparatus according to a sixth aspect of the present invention is the refrigeration apparatus according to the fifth aspect , wherein the third detector is a liquid pipe temperature sensor provided on the outflow side of the radiator, and the control unit Using the temperature obtained by subtracting the correction value corresponding to the heat loss from the sensor mounting position to the expansion mechanism from the detection temperature of the liquid pipe temperature sensor as the refrigerant temperature on the inflow side of the expansion mechanism, the inflow of the use side heat exchanger It can be determined whether or not the side refrigerant is in a supercooled state.

観点に係る冷凍装置では、利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かの判断に、従来からある熱源側液管温度センサを用いることができる。 In the refrigeration apparatus according to the sixth aspect , a conventional heat source side liquid tube temperature sensor can be used to determine whether or not the refrigerant on the inflow side of the use side heat exchanger is in a supercooled state.

本発明の第観点に係る冷凍装置は、第観点又は第観点の冷凍装置において、第1検出器は、圧縮機の吸入側の圧力を検知する吸入圧力センサであり、制御部は、吸入圧力センサによって検出される圧力から圧力飽和温度を算出し得る。 In the refrigeration apparatus according to the seventh aspect of the present invention, in the refrigeration apparatus according to the fifth aspect or the sixth aspect , the first detector is an intake pressure sensor that detects the pressure on the intake side of the compressor, and the control unit includes: The pressure saturation temperature can be calculated from the pressure detected by the suction pressure sensor.

観点に係る冷凍装置では、制御部は、吸入圧力センサによって検出される圧力から圧力飽和温度を算出し得るので、従来からある吸入圧力センサを用いることができる。 In the refrigeration apparatus according to the seventh aspect , since the control unit can calculate the pressure saturation temperature from the pressure detected by the suction pressure sensor, a conventional suction pressure sensor can be used.

第1観点、第2観点又は第3観点に係る冷凍装置では、蒸発器の過熱度制御ができなくなる状況を回避して蒸発器の過熱度の制御を適切に行なわせることができ、蒸発器の手前で冷媒が過冷却状態になり易い冷凍装置の過熱度制御を適切に行わせることができる。 In the refrigeration apparatus according to the first aspect , the second aspect, or the third aspect, it is possible to appropriately control the superheat degree of the evaporator while avoiding the situation where the superheat degree control of the evaporator cannot be performed. It is possible to appropriately perform the superheat degree control of the refrigeration apparatus in which the refrigerant is likely to be in a supercooled state before this.

観点に係る冷凍装置では、利用側熱交換器の過熱度制御ができなくなる状況を回避して利用側熱交換器の過熱度の制御を適切に行なわせることができ、利用側熱交換器の手前で冷媒が過冷却状態になり易い冷凍装置の過熱度制御を適切に行わせることができる。 In the refrigeration apparatus according to the fourth aspect, it is possible to appropriately control the superheat degree of the use side heat exchanger while avoiding the situation where the superheat degree control of the use side heat exchanger cannot be performed. Therefore, it is possible to appropriately perform superheat degree control of the refrigeration apparatus in which the refrigerant is likely to be in a supercooled state.

観点に係る冷凍装置では、正確に過冷却状態の判断を行なうことができ、蒸発器の手前で冷媒が過冷却状態になる冷凍装置の過熱度制御を適切に行わせることができる。 In the refrigeration apparatus according to the fifth aspect , the supercooling state can be accurately determined, and the superheat degree control of the refrigeration apparatus in which the refrigerant is supercooled before the evaporator can be appropriately performed.

観点に係る冷凍装置では、従来からある熱源側液管温度センサを用いることができるので、コストの上昇を抑制できる。 In the refrigeration apparatus according to the sixth aspect , since a conventional heat source side liquid pipe temperature sensor can be used, an increase in cost can be suppressed.

観点に係る冷凍装置では、従来からある吸入圧力センサを用いることができるので、コストの上昇を抑制できる。 In the refrigeration apparatus according to the seventh aspect , since a conventional suction pressure sensor can be used, an increase in cost can be suppressed.

一実施形態に係る冷凍装置を含む空気調和装置の冷媒配管系統を示す図。The figure which shows the refrigerant | coolant piping system of the air conditioning apparatus containing the freezing apparatus which concerns on one Embodiment. 図1の空気調和装置の制御系統を示すブロック図。The block diagram which shows the control system of the air conditioning apparatus of FIG. 冷凍回路の動作を説明するためのグラフ。The graph for demonstrating operation | movement of a freezing circuit.

(1)空気調和装置の全体構成
図1は、本発明の一実施形態に係る冷凍装置を含む空気調和装置の冷媒配管系統を示している。空気調和装置1は、冷媒配管方式の分散型の空気調和装置であって、蒸気圧縮式の冷凍サイクル運転を行うことによって建物内の各室の冷暖房に使用される装置である。空気調和装置1は、熱源ユニットとしての空調室外機2と、利用ユニットとしての複数台(図1では、空調室内機4aおよび空調室内機4bの2台)の空調室内機4と、空調室外機2と空調室内機4とを接続する冷媒連絡管としての第1冷媒連絡管6および第2冷媒連絡管7とを備えている。
(1) Whole structure of air conditioning apparatus FIG. 1: has shown the refrigerant | coolant piping system | strain of the air conditioning apparatus containing the freezing apparatus which concerns on one Embodiment of this invention. The air conditioner 1 is a distributed type air conditioner using a refrigerant piping system, and is an apparatus used for cooling and heating each room in a building by performing a vapor compression refrigeration cycle operation. The air conditioner 1 includes an air conditioner outdoor unit 2 as a heat source unit, a plurality of air conditioner indoor units 4 (in FIG. 1, two units of an air conditioner indoor unit 4a and an air conditioner indoor unit 4b), and an air conditioner outdoor unit. 1 and the 2nd refrigerant | coolant communication pipe | tube 7 as a refrigerant | coolant communication pipe | tube which connects 2 and the air-conditioning indoor unit 4 are provided.

空気調和装置1の冷凍装置10は、空調室外機2と、空調室内機4と、冷媒連絡管6、7とが接続されることによって構成されている。そして、冷凍装置10内には冷媒が封入されており、後述のように、冷媒が圧縮され、冷却され、減圧され、加熱・蒸発された後に、再び圧縮されるという冷凍サイクル運転が行われるようになっている。冷媒としては、例えば、R410A、R407C、R22、R134a、二酸化炭素、などから選択されたものが用いられる。   The refrigeration apparatus 10 of the air conditioner 1 is configured by connecting an air conditioning outdoor unit 2, an air conditioning indoor unit 4, and refrigerant communication pipes 6 and 7. The refrigerant is sealed in the refrigeration apparatus 10, and as described later, the refrigerant is compressed, cooled, depressurized, heated and evaporated, and then compressed again. It has become. As the refrigerant, for example, one selected from R410A, R407C, R22, R134a, carbon dioxide, and the like is used.

(2)空気調和装置の詳細構成
(2−1)空調室内機
空調室内機は、ビル等の室内の天井に埋め込みや吊り下げ等により、又は、室内の壁面に壁掛け等により設置される。空調室内機4は、冷媒連絡管6、7を介して空調室外機2に接続されており、冷凍装置10の一部を構成している。
(2) Detailed configuration of air conditioner (2-1) Air-conditioning indoor unit The air-conditioning indoor unit is installed by being embedded or suspended in the ceiling of a room such as a building, or by hanging on a wall surface of the room. The air conditioning indoor unit 4 is connected to the air conditioning outdoor unit 2 via the refrigerant communication pipes 6 and 7 and constitutes a part of the refrigeration apparatus 10.

次に、空調室内機4の構成について説明する。なお、空調室内機4として、図1では空調室内機4a,4bの2台を示しているが、いずれの空調室内機4もほぼ同じ構成であるため、ここでは、空調室内機4aの構成のみを説明する。   Next, the configuration of the air conditioning indoor unit 4 will be described. In FIG. 1, two air conditioning indoor units 4a and 4b are shown as the air conditioning indoor unit 4. However, since each of the air conditioning indoor units 4 has almost the same configuration, only the configuration of the air conditioning indoor unit 4a is shown here. Will be explained.

空調室内機4aは、冷凍装置10の一部を構成する室内側主冷媒回路10aを有している。室内側主冷媒回路10aは、主として、減圧器である室内膨張弁41と、利用側熱交換器としての室内熱交換器42とを有している。   The air conditioning indoor unit 4 a has an indoor main refrigerant circuit 10 a that constitutes a part of the refrigeration apparatus 10. The indoor main refrigerant circuit 10a mainly includes an indoor expansion valve 41 that is a decompressor and an indoor heat exchanger 42 that is a use-side heat exchanger.

室内膨張弁41は、冷媒を減圧するための機構であり、開度調整が可能な電動弁である。室内膨張弁41は、その一端が第1冷媒連絡管6に接続され、その他端が室内熱交換器42に接続されている。   The indoor expansion valve 41 is a mechanism for reducing the pressure of the refrigerant, and is an electric valve capable of adjusting the opening degree. The indoor expansion valve 41 has one end connected to the first refrigerant communication pipe 6 and the other end connected to the indoor heat exchanger 42.

室内熱交換器42は、例えば伝熱管と多数のフィンとにより構成されたクロスフィン式のフィン・アンド・チューブ型熱交換器であり、冷房運転時には冷媒の蒸発器として機能して室内空気を冷却し、暖房運転時には冷媒の凝縮器として機能して室内空気を加熱する熱交換器である。室内熱交換器42は、その一端が室内膨張弁41に接続され、その他端が第2冷媒連絡管7に接続されている。   The indoor heat exchanger 42 is, for example, a cross fin type fin-and-tube heat exchanger composed of heat transfer tubes and a large number of fins, and functions as a refrigerant evaporator during cooling operation to cool indoor air. In the heating operation, the heat exchanger functions as a refrigerant condenser and heats indoor air. The indoor heat exchanger 42 has one end connected to the indoor expansion valve 41 and the other end connected to the second refrigerant communication tube 7.

空調室内機4aは、ユニット内に室内空気を吸入して、再び室内に供給するための室内ファン43を備えており、室内空気と室内熱交換器42を流れる冷媒との間で熱交換をさせる。室内ファン43は、室内熱交換器42に供給する空気の風量を可変することが可能なファンであり、DCファンモータ等からなる室内ファン用モータ43aによって回転駆動される。室内ファン43では、室内熱交換器42に送風するために室内ファン用モータ43aにより例えば遠心ファンや多翼ファン等が駆動される。   The air conditioning indoor unit 4a includes an indoor fan 43 for sucking indoor air into the unit and supplying the indoor air again, and exchanges heat between the indoor air and the refrigerant flowing through the indoor heat exchanger 42. . The indoor fan 43 is a fan capable of changing the air volume of air supplied to the indoor heat exchanger 42, and is rotationally driven by an indoor fan motor 43a including a DC fan motor. In the indoor fan 43, for example, a centrifugal fan or a multi-blade fan is driven by the indoor fan motor 43a in order to send air to the indoor heat exchanger.

また、空調室内機4aには、各種のセンサが設けられている。具体的には、サーミスタからなる室内液管温度センサ44や室内ガス管温度センサ45が設けられ、室内熱交換器42に近接する冷媒配管の温度から冷媒の温度を測定する。また、室内温度センサ46が設けられており、この室内温度センサ46は熱交換が行われる前の空調室内機4に吸入される室内空気の温度を検出する。さらに、空調室内機4aは、空調室内機4aを構成する各部の動作を制御する室内制御装置47を有している。室内制御装置47は、空調室内機4aの制御を行うために設けられたマイクロコンピュータやメモリ等を有しており、空調室内機4aを個別に操作するためのリモートコントローラ(図示せず)との間で制御信号等のやりとりを行ったり、後述する空調室外機2の室外制御装置30との間で伝送線8aを介して制御信号等のやりとりを行ったりする。   The air conditioning indoor unit 4a is provided with various sensors. Specifically, an indoor liquid pipe temperature sensor 44 and an indoor gas pipe temperature sensor 45 each including a thermistor are provided, and the temperature of the refrigerant is measured from the temperature of the refrigerant pipe adjacent to the indoor heat exchanger 42. Moreover, the indoor temperature sensor 46 is provided, This indoor temperature sensor 46 detects the temperature of the indoor air inhaled by the air-conditioning indoor unit 4 before heat exchange is performed. Furthermore, the air conditioning indoor unit 4a has an indoor control device 47 that controls the operation of each part constituting the air conditioning indoor unit 4a. The indoor control device 47 has a microcomputer, a memory, and the like provided for controlling the air conditioning indoor unit 4a, and a remote controller (not shown) for individually operating the air conditioning indoor unit 4a. Control signals and the like are exchanged between them, and control signals and the like are exchanged with the outdoor control device 30 of the air conditioner outdoor unit 2 described later via the transmission line 8a.

(2−2)空調室外機
空調室外機2は、ビル等の室外に設置されており、第1冷媒連絡管6及び第2冷媒連絡管7を介して空調室内機4a、4bに接続されている。空調室外機2は、冷凍装置10の一部を構成する室外側主冷媒回路10cと冷凍装置10から分岐する過冷却用冷媒流路61とを有している。
(2-2) Air-conditioning outdoor unit The air-conditioning outdoor unit 2 is installed outside a building or the like, and is connected to the air-conditioning indoor units 4a and 4b via the first refrigerant communication pipe 6 and the second refrigerant communication pipe 7. Yes. The air conditioning outdoor unit 2 includes an outdoor main refrigerant circuit 10 c that constitutes a part of the refrigeration apparatus 10 and a supercooling refrigerant flow path 61 that branches from the refrigeration apparatus 10.

(2−2−1)室外側主冷媒回路
室外側主冷媒回路10cは、主として、圧縮機21と、切換機構22と、室外熱交換器23と、室外第1膨張弁25と、液ガス熱交換器27と、液側閉鎖弁28aと、ガス側閉鎖弁28bと、アキュムレータ29とを有している。この室外側主冷媒回路10cは、主として、圧縮機21と、切換機構22と、熱源側熱交換器としての室外熱交換器23と、第2遮断機構又は熱源側膨張機構としての室外第1膨張弁25と、温度調節機構としての液ガス熱交換器27と、第1遮断機構としての液側閉鎖弁28aと、ガス側閉鎖弁28bとを有している。
(2-2-1) Outdoor Main Refrigerant Circuit The outdoor main refrigerant circuit 10c mainly includes the compressor 21, the switching mechanism 22, the outdoor heat exchanger 23, the outdoor first expansion valve 25, and liquid gas heat. It has an exchanger 27, a liquid side closing valve 28 a, a gas side closing valve 28 b, and an accumulator 29. The outdoor main refrigerant circuit 10c mainly includes a compressor 21, a switching mechanism 22, an outdoor heat exchanger 23 as a heat source side heat exchanger, and an outdoor first expansion as a second shut-off mechanism or a heat source side expansion mechanism. It has a valve 25, a liquid gas heat exchanger 27 as a temperature adjusting mechanism, a liquid side closing valve 28a as a first shut-off mechanism, and a gas side closing valve 28b.

圧縮機21は、圧縮機用モータ21aによって駆動される密閉式圧縮機である。圧縮機用モータ21aが例えばインバータにより回転数が制御され、圧縮機21は、運転容量を可変することができるよう構成されている。   The compressor 21 is a hermetic compressor driven by a compressor motor 21a. The rotation speed of the compressor motor 21a is controlled by, for example, an inverter, and the compressor 21 is configured to be able to vary the operating capacity.

切換機構22は、冷媒の流れの方向を切り換えるための機構である。冷房運転時には、室外熱交換器23を圧縮機21によって圧縮される冷媒の放熱器として機能させ、かつ、室内熱交換器42を室外熱交換器23において冷却された冷媒の蒸発器として機能させる。このために、切換機構22は、圧縮機21の吐出側の冷媒配管と室外熱交換器23の一端とを接続するとともに、圧縮機吸入側配管29a(アキュムレータ29を含む)とガス側閉鎖弁28bとを接続する(図1の切換機構22の実線を参照)。また、切換機構22は、暖房運転時には、室内熱交換器42を圧縮機21によって圧縮される冷媒の放熱器として機能させ、かつ、室外熱交換器23を室内熱交換器42において冷却された冷媒の蒸発器として機能させる。このために、切換機構22は、圧縮機21の吐出側の冷媒配管とガス側閉鎖弁28bとを接続するとともに、圧縮機吸入側配管29aと室外熱交換器23の一端とを接続する(図1の切換機構22の破線を参照)。切換機構22は、例えば四路切換弁である。   The switching mechanism 22 is a mechanism for switching the direction of the refrigerant flow. During the cooling operation, the outdoor heat exchanger 23 functions as a radiator for the refrigerant compressed by the compressor 21, and the indoor heat exchanger 42 functions as an evaporator for the refrigerant cooled in the outdoor heat exchanger 23. For this purpose, the switching mechanism 22 connects the refrigerant pipe on the discharge side of the compressor 21 and one end of the outdoor heat exchanger 23, and also connects the compressor suction side pipe 29a (including the accumulator 29) and the gas side closing valve 28b. (See the solid line of the switching mechanism 22 in FIG. 1). Further, the switching mechanism 22 causes the indoor heat exchanger 42 to function as a radiator for the refrigerant compressed by the compressor 21 during the heating operation, and the outdoor heat exchanger 23 is cooled by the indoor heat exchanger 42. To function as an evaporator. For this purpose, the switching mechanism 22 connects the refrigerant pipe on the discharge side of the compressor 21 and the gas side shut-off valve 28b, and connects the compressor suction side pipe 29a and one end of the outdoor heat exchanger 23 (FIG. 1 (see the broken line of the switching mechanism 22). The switching mechanism 22 is, for example, a four-way switching valve.

室外熱交換器23は、伝熱管と多数のフィンとから構成されるクロスフィン式のフィン・アンド・チューブ型熱交換器であり、その一端が切換機構22に接続されており、その他端が室外第1膨張弁25に接続されている。   The outdoor heat exchanger 23 is a cross fin type fin-and-tube heat exchanger composed of heat transfer tubes and a large number of fins, one end of which is connected to the switching mechanism 22 and the other end of the outdoor heat exchanger 23. The first expansion valve 25 is connected.

空調室外機2は、ユニット内に室外空気を吸入して、再び室外に排出するための室外ファン26を有している。室外ファン26は、室外空気と室外熱交換器23を流れる冷媒との間で熱交換をさせる。   The air conditioner outdoor unit 2 has an outdoor fan 26 for sucking outdoor air into the unit and discharging it to the outdoor again. The outdoor fan 26 exchanges heat between the outdoor air and the refrigerant flowing through the outdoor heat exchanger 23.

室外第1膨張弁25は、冷凍装置10において冷媒を減圧するための機構であり、開度調整が可能な電動弁である。室外第1膨張弁25は、室外側主冷媒回路10c内を流れる冷媒の圧力や流量等の調節を行うために、冷房運転を行う際の冷凍装置10における冷媒の流れ方向において室外熱交換器23の下流側であって液ガス熱交換器27の上流側に配置され、冷媒の通過を遮断することも可能である。室外第1膨張弁25は、その一端が室外熱交換器23に接続され、その他端が液ガス熱交換器27を介して液側閉鎖弁28aに接続され、室内熱交換器42の液側に接続されている。   The outdoor first expansion valve 25 is a mechanism for decompressing the refrigerant in the refrigeration apparatus 10, and is an electric valve capable of adjusting the opening degree. The outdoor first expansion valve 25 is configured to adjust the pressure, flow rate, and the like of the refrigerant flowing in the outdoor main refrigerant circuit 10c in the outdoor heat exchanger 23 in the refrigerant flow direction in the refrigeration apparatus 10 during the cooling operation. It is also possible to block the passage of the refrigerant by being arranged on the downstream side of the gas and upstream of the liquid gas heat exchanger 27. One end of the outdoor first expansion valve 25 is connected to the outdoor heat exchanger 23, and the other end is connected to the liquid side shut-off valve 28 a via the liquid gas heat exchanger 27, and is connected to the liquid side of the indoor heat exchanger 42. It is connected.

空調室外機2は、ユニット内に室外空気を吸入して、室外熱交換器23において冷媒と熱交換させた後に、室外に排出するための送風ファンとしての室外ファン26を有している。この室外ファン26は、室外熱交換器23に供給する空気の風量を可変することが可能なファンであり、例えば、DCファンモータ等からなるモータ26aによって駆動されるプロペラファン等である。   The air-conditioning outdoor unit 2 has an outdoor fan 26 as a blower fan for sucking outdoor air into the unit and exchanging heat with the refrigerant in the outdoor heat exchanger 23 and then discharging it to the outside. The outdoor fan 26 is a fan capable of changing the air volume supplied to the outdoor heat exchanger 23, and is, for example, a propeller fan driven by a motor 26a composed of a DC fan motor or the like.

液ガス熱交換器27は、室外第1膨張弁25と液側閉鎖弁28aとの間に接続されている。液ガス熱交換器27は、熱源側熱交換器において凝縮された冷媒が流れる冷媒管と後述の分岐管64とを接触させる二重管構造を持つ配管熱交換器である。液ガス熱交換器27は、冷凍装置10を室外熱交換器23から空調室内機4に向かって流れる冷媒と、過冷却用冷媒流路61を室外第2膨張弁62から圧縮機吸入側配管29aへと流れる冷媒との間で熱交換を行わせる。それにより、液ガス熱交換器27は、この熱交換によって、冷房運転時に室外熱交換器23において凝縮された冷媒をさらに冷却し、空調室内機4へと向かう冷媒の過冷却度を大きくする。   The liquid gas heat exchanger 27 is connected between the outdoor first expansion valve 25 and the liquid side closing valve 28a. The liquid gas heat exchanger 27 is a pipe heat exchanger having a double-pipe structure in which a refrigerant pipe through which the refrigerant condensed in the heat source side heat exchanger flows and a branch pipe 64 described later are brought into contact with each other. The liquid gas heat exchanger 27 includes a refrigerant that flows in the refrigeration apparatus 10 from the outdoor heat exchanger 23 toward the air conditioning indoor unit 4, and a supercooling refrigerant flow path 61 from the outdoor second expansion valve 62 to the compressor suction side pipe 29a. Heat exchange with the refrigerant flowing into the Thereby, the liquid gas heat exchanger 27 further cools the refrigerant condensed in the outdoor heat exchanger 23 during the cooling operation by this heat exchange, and increases the degree of supercooling of the refrigerant toward the air conditioning indoor unit 4.

アキュムレータ29は、切換機構22と圧縮機21との間の圧縮機吸入側配管29aに配置されている。   The accumulator 29 is disposed in a compressor suction side pipe 29 a between the switching mechanism 22 and the compressor 21.

(2−2−2)過冷却用冷媒流路
過冷却用冷媒流路61は、室外第2膨張弁62から液ガス熱交換器27を経て、切換機構22とアキュムレータ29との間の圧縮機吸入側配管29aへ向かう冷媒管で構成されている。室外第2膨張弁62は、過冷却用冷媒流路61において冷媒を減圧するための機構であり、開度調整が可能な電動弁である。室外第2膨張弁62は、過冷却用冷媒流路61に設けられ、過冷却用冷媒流路61において室外第1膨張弁25から液側閉鎖弁28aにつながる配管から分岐して液ガス熱交換器27に入るまでの間に配置されている。
(2-2-2) Supercooling Refrigerant Channel The supercooling refrigerant channel 61 is a compressor between the switching mechanism 22 and the accumulator 29 via the liquid gas heat exchanger 27 from the outdoor second expansion valve 62. It is comprised with the refrigerant | coolant pipe | tube toward the suction side piping 29a. The outdoor second expansion valve 62 is a mechanism for decompressing the refrigerant in the supercooling refrigerant flow path 61, and is an electric valve capable of adjusting the opening degree. The outdoor second expansion valve 62 is provided in the supercooling refrigerant flow path 61, and in the supercooling refrigerant flow path 61 branches from a pipe connected from the outdoor first expansion valve 25 to the liquid side closing valve 28a to exchange liquid gas heat. It is arranged until the container 27 is entered.

液ガス熱交換器27には、冷却源としての分岐管64が設けられている。なお、冷凍装置10から過冷却用冷媒流路61を除いた部分が主冷媒回路である。過冷却用冷媒流路61は、液ガス熱交換器27と室外第1膨張弁25との間で分岐される冷媒を圧縮機21の吸入側に戻すように主冷媒回路に接続されている。過冷却用冷媒流路61で分岐された冷媒は、減圧された後に、液ガス熱交換器27に導入される。そして、過冷却用冷媒流路61で分岐された冷媒は、室外熱交換器23から第1冷媒連絡管6を通じて室内膨張弁41に送られる冷媒と熱交換させた後に、圧縮機21の吸入側に戻される。   The liquid gas heat exchanger 27 is provided with a branch pipe 64 as a cooling source. A portion of the refrigeration apparatus 10 excluding the supercooling refrigerant flow path 61 is a main refrigerant circuit. The supercooling refrigerant channel 61 is connected to the main refrigerant circuit so as to return the refrigerant branched between the liquid gas heat exchanger 27 and the outdoor first expansion valve 25 to the suction side of the compressor 21. The refrigerant branched in the supercooling refrigerant passage 61 is decompressed and then introduced into the liquid gas heat exchanger 27. The refrigerant branched in the supercooling refrigerant flow path 61 is subjected to heat exchange with the refrigerant sent from the outdoor heat exchanger 23 to the indoor expansion valve 41 through the first refrigerant communication pipe 6, and then the suction side of the compressor 21. Returned to

さらに詳細に見ると、過冷却用冷媒流路61は、分岐管64と合流管65と室外第2膨張弁62を有している。分岐管64は、室外第1膨張弁25から室内膨張弁41に送られる冷媒の一部を室外熱交換器23と液ガス熱交換器27との間の位置から分岐されるように接続されている。合流管65は、液ガス熱交換器27の過冷却用冷媒流路側の出口から圧縮機21の吸入側に戻すように圧縮機21の吸入側に接続されている。室外第2膨張弁62は、電動膨張弁からなり、過冷却用冷媒流路61を流れる冷媒の流量を調節するための連通管膨張機構として機能する。これにより、室外熱交換器23から室内膨張弁41に送られる冷媒は、液ガス熱交換器27において、室外第2膨張弁62によって減圧された後の過冷却用冷媒流路61を流れる冷媒によって冷却される。すなわち、液ガス熱交換器27は、室外第2膨張弁62の開度調節によって能力制御が行われることになる。   More specifically, the supercooling refrigerant flow path 61 includes a branch pipe 64, a junction pipe 65, and an outdoor second expansion valve 62. The branch pipe 64 is connected so that a part of the refrigerant sent from the outdoor first expansion valve 25 to the indoor expansion valve 41 is branched from a position between the outdoor heat exchanger 23 and the liquid gas heat exchanger 27. Yes. The junction pipe 65 is connected to the suction side of the compressor 21 so as to return to the suction side of the compressor 21 from the outlet on the supercooling refrigerant flow path side of the liquid gas heat exchanger 27. The outdoor second expansion valve 62 is an electric expansion valve, and functions as a communication pipe expansion mechanism for adjusting the flow rate of the refrigerant flowing through the supercooling refrigerant flow path 61. Thereby, the refrigerant sent from the outdoor heat exchanger 23 to the indoor expansion valve 41 is caused by the refrigerant flowing in the subcooling refrigerant flow path 61 after being depressurized by the outdoor second expansion valve 62 in the liquid gas heat exchanger 27. To be cooled. That is, the capacity control of the liquid gas heat exchanger 27 is performed by adjusting the opening degree of the outdoor second expansion valve 62.

また、過冷却用冷媒流路61は、後述のように、冷凍装置10のうち液側閉鎖弁28aと室外第1膨張弁25との間の部分と圧縮機21の吸入側の部分とを接続する連通管としても機能するようになっている。   Further, as described later, the supercooling refrigerant flow path 61 connects a portion of the refrigeration apparatus 10 between the liquid side closing valve 28a and the outdoor first expansion valve 25 and a suction side portion of the compressor 21. It is designed to function as a communication pipe.

液側閉鎖弁28a及びガス側閉鎖弁28bは、外部の機器・配管(具体的には、第1冷媒連絡管6及び第2冷媒連絡管7)との接続口に設けられた弁である。液側閉鎖弁28aは、液ガス熱交換器27に接続され、ガス側閉鎖弁28bは、切換機構22に接続され、これらによって冷媒の通過を遮断することができる。   The liquid side shutoff valve 28a and the gas side shutoff valve 28b are valves provided at connection ports with external devices and pipes (specifically, the first refrigerant communication pipe 6 and the second refrigerant communication pipe 7). The liquid side shut-off valve 28a is connected to the liquid gas heat exchanger 27, and the gas side shut-off valve 28b is connected to the switching mechanism 22, thereby blocking the passage of the refrigerant.

(2−2−3)室外制御装置と各種センサ
空調室外機2は、空調室外機2を構成する各部の動作を制御する室外制御装置30を有している。そして、室外制御装置30は、空調室外機2の制御を行うために設けられたマイクロコンピュータ、メモリやモータ26aを制御するインバータ回路等を有しており、空調室内機4a,4bの室内制御装置47との間で伝送線8aを介して制御信号等のやりとりを行うことができるようになっている。すなわち、室内制御装置47と室外制御装置30と室内制御装置47間を接続する伝送線8aとによって、空気調和装置1全体の運転制御を行う空調制御装置8が構成されている。
(2-2-3) Outdoor Control Device and Various Sensors The air-conditioning outdoor unit 2 has an outdoor control device 30 that controls the operation of each part constituting the air-conditioning outdoor unit 2. The outdoor control device 30 includes a microcomputer provided for controlling the air conditioning outdoor unit 2, a memory, an inverter circuit for controlling the motor 26a, and the like, and the indoor control devices for the air conditioning indoor units 4a and 4b. Control signals and the like can be exchanged with the terminal 47 via the transmission line 8a. That is, the indoor control device 47, the outdoor control device 30, and the transmission line 8a connecting the indoor control devices 47 constitute the air conditioning control device 8 that controls the operation of the entire air conditioner 1.

また、空調室外機2には、各種のセンサが設けられている。圧縮機21の吐出側の冷媒配管には、圧縮機吐出圧力を検出する吐出圧力センサ31と、圧縮機吐出温度を検出する吐出温度センサ32とが設けられている。圧縮機吸入側配管29aには、圧縮機21に吸入されるガス冷媒の温度を検出する吸入温度センサ34と、圧縮機吸入圧力を検出する吸入圧力センサ33とが設けられている。室外制御装置30は、圧縮機21の運転容量を制御するように構成されており、冷房運転中における圧縮機21の吸入圧力の目標値である低圧目標値及び暖房運転中における圧縮機21の吐出圧力の目標値である高圧目標値を有している。そして、冷房運転時には吸入圧力センサ33が低圧目標値となるように圧縮機21の運転容量が制御され、暖房運転時には吐出圧力センサ31が高圧目標値になるように圧縮機21の運転容量が制御される。   The air conditioner outdoor unit 2 is provided with various sensors. The refrigerant pipe on the discharge side of the compressor 21 is provided with a discharge pressure sensor 31 that detects the compressor discharge pressure and a discharge temperature sensor 32 that detects the compressor discharge temperature. The compressor suction side pipe 29a is provided with a suction temperature sensor 34 for detecting the temperature of the gas refrigerant sucked into the compressor 21 and a suction pressure sensor 33 for detecting the compressor suction pressure. The outdoor control device 30 is configured to control the operation capacity of the compressor 21, and is a low pressure target value that is a target value of the suction pressure of the compressor 21 during the cooling operation and a discharge of the compressor 21 during the heating operation. It has a high pressure target value that is a target value of pressure. The operating capacity of the compressor 21 is controlled so that the suction pressure sensor 33 becomes the low pressure target value during the cooling operation, and the operating capacity of the compressor 21 is controlled so that the discharge pressure sensor 31 becomes the high pressure target value during the heating operation. Is done.

また、液ガス熱交換器27の主冷媒回路側の出口には、冷媒の温度(すなわち、液管温度)を検出する液管温度センサ35が設けられている。空調室外機2の室外空気の吸込口側には、内部に流入する室外空気の温度(すなわち、室外温度)を検出する室外温度センサ36が設けられている。液ガス熱交換器27から、切換機構22とアキュムレータ29との間の低圧冷媒配管へ向かう、過冷却用冷媒流路61の合流管65には、液ガス熱交換器27の過冷却用冷媒流路側の出口を流れる冷媒の温度を検出するためのバイパス温度センサ63が設けられている。これら、吐出温度センサ32、吸入温度センサ34、液管温度センサ35、室外温度センサ36及びバイパス温度センサ63は、サーミスタからなる。   Further, a liquid pipe temperature sensor 35 for detecting the temperature of the refrigerant (that is, the liquid pipe temperature) is provided at the outlet of the liquid gas heat exchanger 27 on the main refrigerant circuit side. An outdoor temperature sensor 36 for detecting the temperature of the outdoor air flowing into the inside (that is, the outdoor temperature) is provided on the outdoor air suction side of the air conditioning outdoor unit 2. From the liquid gas heat exchanger 27 to the low-pressure refrigerant pipe between the switching mechanism 22 and the accumulator 29, a supercooling refrigerant flow of the liquid gas heat exchanger 27 flows into the merge pipe 65 of the supercooling refrigerant flow path 61. A bypass temperature sensor 63 for detecting the temperature of the refrigerant flowing through the roadside outlet is provided. The discharge temperature sensor 32, the suction temperature sensor 34, the liquid pipe temperature sensor 35, the outdoor temperature sensor 36, and the bypass temperature sensor 63 are composed of thermistors.

(2−3)冷媒連絡管
冷媒連絡管6、7は、空調室外機2および空調室内機4を設置場所に設置する際に、現地にて施工される冷媒配管である。第1冷媒連絡管6は、空調室外機2及び空調室内機4a、4bに接続されており、冷房運転時には、液ガス熱交換器27において過冷却度が大きくなった液冷媒を室内膨張弁41および室内熱交換器42に送り、暖房運転時には、室内熱交換器42において凝縮した液冷媒を空調室外機2の室外熱交換器23に送る冷媒管である。第2冷媒連絡管7は、空調室外機2及び空調室内機4a、4bに接続されており、冷房運転時には、室内熱交換器42において蒸発したガス冷媒を空調室外機2の圧縮機21に送り、暖房運転時には、圧縮機21において圧縮されたガス冷媒を空調室内機4a,4bの室内熱交換器42に送る冷媒管である。
(2-3) Refrigerant communication pipes The refrigerant communication pipes 6 and 7 are refrigerant pipes constructed on site when the air-conditioning outdoor unit 2 and the air-conditioning indoor unit 4 are installed at the installation location. The first refrigerant communication pipe 6 is connected to the air-conditioning outdoor unit 2 and the air-conditioning indoor units 4a and 4b. During the cooling operation, the liquid refrigerant whose degree of supercooling in the liquid gas heat exchanger 27 is increased to the indoor expansion valve 41. And a refrigerant pipe that sends the liquid refrigerant condensed in the indoor heat exchanger 42 to the outdoor heat exchanger 23 of the air conditioning outdoor unit 2 during heating operation. The second refrigerant communication pipe 7 is connected to the air-conditioning outdoor unit 2 and the air-conditioning indoor units 4a and 4b, and sends the gas refrigerant evaporated in the indoor heat exchanger 42 to the compressor 21 of the air-conditioning outdoor unit 2 during the cooling operation. In the heating operation, the refrigerant pipes send the gas refrigerant compressed in the compressor 21 to the indoor heat exchangers 42 of the air conditioning indoor units 4a and 4b.

(2−4)空調制御装置
図2に、空気調和装置1の制御ブロック図を示す。空気調和装置1の各種運転制御を行う制御手段としての空調制御装置8は、図2に示すように伝送線8aを介して結ばれる室外制御装置30および室内制御装置47によって構成されている。空調制御装置8は、各種センサ31〜36,44〜46,63の検出信号を受け、これらの検出信号等に基づいて各種機器21,22,25、26,41,43,62を制御する。
(2-4) Air Conditioning Control Device FIG. 2 shows a control block diagram of the air conditioner 1. The air conditioning control device 8 as a control means for performing various operation controls of the air conditioner 1 is configured by an outdoor control device 30 and an indoor control device 47 connected via a transmission line 8a as shown in FIG. The air conditioning control device 8 receives the detection signals of the various sensors 31 to 36, 44 to 46, 63, and controls the various devices 21, 22, 25, 26, 41, 43, 62 based on these detection signals and the like.

(3)空気調和装置の動作
次に、本実施形態に係る空気調和装置1の基本的な動作について説明する。なお、以下に説明する各種運転における制御は空調制御装置8によって行われる。
(3) Operation of Air Conditioner Next, the basic operation of the air conditioner 1 according to the present embodiment will be described. Note that control in various operations described below is performed by the air conditioning control device 8.

(3−1)冷房運転
冷凍サイクルにおける高圧と低圧の差が小さい低差圧にて運転している空気調和装置においては、例えば冷媒充填量が多くかつ外気温が低い場合に蒸発温度を上げる運転を行うと、蒸発器として機能している室内熱交換器42の手前で冷媒が過冷却状態となることがある。以下の説明では、室内熱交換器42の手前で過冷却状態になっていないときの運転を通常時の冷房運転とよび、過冷却状態になっているときの運転を異常時の冷房運転とよんで両者を区別して説明する。
(3-1) Cooling operation In an air conditioner operating at a low differential pressure where the difference between the high pressure and the low pressure in the refrigeration cycle is small, for example, an operation that raises the evaporation temperature when the refrigerant charge amount is large and the outside air temperature is low As a result, the refrigerant may be supercooled before the indoor heat exchanger 42 functioning as an evaporator. In the following description, the operation when the subcooling state is not in front of the indoor heat exchanger 42 is referred to as a normal cooling operation, and the operation when the subcooling state is referred to as an abnormal cooling operation. Both will be described separately.

(3−1−1)通常時の冷房運転
冷房運転時は、切換機構22が図1の実線で示される状態、すなわち、圧縮機21の吐出側が室外熱交換器23のガス側に接続され、かつ、圧縮機21の吸入側がガス側閉鎖弁28b及び第2冷媒連絡管7を介して室内熱交換器42のガス側に接続された状態となっている。冷房運転時、室外第1膨張弁25は全開状態にされ、液側閉鎖弁28a及びガス側閉鎖弁28bは開状態にされている。
(3-1-1) Cooling operation at normal time During the cooling operation, the switching mechanism 22 is in the state shown by the solid line in FIG. 1, that is, the discharge side of the compressor 21 is connected to the gas side of the outdoor heat exchanger 23, In addition, the suction side of the compressor 21 is connected to the gas side of the indoor heat exchanger 42 via the gas side closing valve 28 b and the second refrigerant communication pipe 7. During the cooling operation, the outdoor first expansion valve 25 is fully opened, and the liquid side closing valve 28a and the gas side closing valve 28b are opened.

各室内膨張弁41は、室内熱交換器42の出口(すなわち、室内熱交換器42のガス側)における冷媒の過熱度が第1過熱度目標値Tsh1で一定になるように開度調節されるようになっている。例えば、図3において、圧力P1の点Cが室内膨張弁41の流入側であり、圧力P2の点Bが室内膨張弁41の流出側である。各室内熱交換器42の出口における冷媒の過熱度は、室内制御装置47において、室内ガス管温度センサ45により検出される冷媒温度Th1から室内液管温度センサ44により検出される冷媒温度Th2を差し引くことによって検出される。   The opening degree of each indoor expansion valve 41 is adjusted so that the superheat degree of the refrigerant at the outlet of the indoor heat exchanger 42 (that is, the gas side of the indoor heat exchanger 42) becomes constant at the first superheat degree target value Tsh1. It is like that. For example, in FIG. 3, the point C of the pressure P1 is the inflow side of the indoor expansion valve 41, and the point B of the pressure P2 is the outflow side of the indoor expansion valve 41. The degree of superheat of the refrigerant at the outlet of each indoor heat exchanger 42 is obtained by subtracting the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 from the refrigerant temperature Th1 detected by the indoor gas pipe temperature sensor 45 in the indoor control device 47. Is detected by

このとき、室内熱交換器42の手前で過冷却状態になっていないことは、室内制御装置47において、室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも高くなっていないこと(Tein≦Th2)を検出することにより判断される。この室内機液管圧力飽和温度Teinは、例えば吸入圧力センサ33により検出される圧縮機21の吸入圧力LPを蒸発温度Teに対応する飽和温度に換算することにより得られる。   At this time, the fact that the subcooling state is not reached before the indoor heat exchanger 42 is that the indoor unit liquid pipe pressure saturation temperature Tein is detected from the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 in the indoor control device 47. Is determined not to be high (Tein ≦ Th2). The indoor unit liquid pipe pressure saturation temperature Tein is obtained, for example, by converting the suction pressure LP of the compressor 21 detected by the suction pressure sensor 33 into a saturation temperature corresponding to the evaporation temperature Te.

また、室外第2膨張弁62は、液ガス熱交換器27の過冷却用冷媒流路側の出口における冷媒の過熱度が過熱度目標値になるように開度調節される(以下、過熱度制御という)。液ガス熱交換器27の過冷却用冷媒流路側の出口における冷媒の過熱度は、吸入圧力センサ33により検出される圧縮機21の吸入圧力が蒸発温度に対応する飽和温度に換算され、バイパス温度センサ63により検出される冷媒温度からこの冷媒の飽和温度を差し引くことによって検出される。   The opening degree of the outdoor second expansion valve 62 is adjusted so that the superheat degree of the refrigerant at the outlet of the liquid gas heat exchanger 27 on the supercooling refrigerant channel side becomes the superheat degree target value (hereinafter, superheat degree control). Called). The degree of superheat of the refrigerant at the outlet of the liquid-gas heat exchanger 27 on the side of the supercooling refrigerant flow path is converted into a saturation temperature corresponding to the evaporation temperature by the suction pressure of the compressor 21 detected by the suction pressure sensor 33, and the bypass temperature. This is detected by subtracting the saturation temperature of the refrigerant from the refrigerant temperature detected by the sensor 63.

この冷凍装置10の状態で、圧縮機21、室外ファン26及び室内ファン43を運転すると、低圧のガス冷媒は、圧縮機21に吸入されて圧縮されて高圧のガス冷媒となる。その後、高圧のガス冷媒は、切換機構22を経由して室外熱交換器23に送られて、室外ファン26によって供給される室外空気と熱交換を行って凝縮して高圧の液冷媒となる。そして、この高圧の液冷媒は、室外第1膨張弁25を通過した後に、液ガス熱交換器27に流入し、過冷却用冷媒流路61を流れる冷媒と熱交換を行ってさらに冷却されて過冷却状態になる。このとき、室外熱交換器23において凝縮した高圧の液冷媒の一部は、過冷却用冷媒流路61に分岐され、室外第2膨張弁62によって減圧された後に、圧縮機21の吸入側に戻される。ここで、室外第2膨張弁62を通過する冷媒は、圧縮機21の吸入圧力近くまで減圧されることで、その一部が蒸発する。そして、過冷却用冷媒流路61の室外第2膨張弁62の出口から圧縮機21の吸入側に向かって流れる冷媒は、液ガス熱交換器27を通過して、主冷媒回路側の室外熱交換器23から空調室内機4へ送られる高圧の液冷媒と熱交換を行う。   When the compressor 21, the outdoor fan 26, and the indoor fan 43 are operated in the state of the refrigeration apparatus 10, the low-pressure gas refrigerant is sucked into the compressor 21 and compressed to become a high-pressure gas refrigerant. Thereafter, the high-pressure gas refrigerant is sent to the outdoor heat exchanger 23 via the switching mechanism 22, exchanges heat with the outdoor air supplied by the outdoor fan 26, and is condensed to become a high-pressure liquid refrigerant. Then, after passing through the outdoor first expansion valve 25, the high-pressure liquid refrigerant flows into the liquid gas heat exchanger 27 and is further cooled by exchanging heat with the refrigerant flowing through the subcooling refrigerant flow path 61. It becomes supercooled. At this time, a part of the high-pressure liquid refrigerant condensed in the outdoor heat exchanger 23 is branched into the subcooling refrigerant flow path 61, and after being decompressed by the outdoor second expansion valve 62, the refrigerant enters the suction side of the compressor 21. Returned. Here, a part of the refrigerant passing through the outdoor second expansion valve 62 is evaporated by being depressurized to near the suction pressure of the compressor 21. Then, the refrigerant flowing from the outlet of the outdoor second expansion valve 62 of the supercooling refrigerant flow path 61 toward the suction side of the compressor 21 passes through the liquid gas heat exchanger 27 and the outdoor heat on the main refrigerant circuit side. Heat exchange is performed with the high-pressure liquid refrigerant sent from the exchanger 23 to the air conditioning indoor unit 4.

そして、過冷却状態になった高圧の液冷媒は、液側閉鎖弁28a及び第1冷媒連絡管6を経由して、空調室内機4に送られる。   The supercooled high-pressure liquid refrigerant is sent to the air conditioning indoor unit 4 via the liquid side closing valve 28 a and the first refrigerant communication pipe 6.

この空調室内機4に送られた高圧の液冷媒は、室内膨張弁41によって圧縮機21の吸入圧力近くまで減圧されて低圧の気液二相状態の冷媒となって室内熱交換器42に送られ、室内熱交換器42において室内空気と熱交換を行って蒸発して低圧のガス冷媒となる。   The high-pressure liquid refrigerant sent to the air-conditioning indoor unit 4 is decompressed to near the suction pressure of the compressor 21 by the indoor expansion valve 41 to become a low-pressure gas-liquid two-phase refrigerant and sent to the indoor heat exchanger 42. In the indoor heat exchanger 42, heat is exchanged with the room air to evaporate to become a low-pressure gas refrigerant.

この低圧のガス冷媒は、第2冷媒連絡管7を経由して空調室外機2に送られ、ガス側閉鎖弁28b及び切換機構22を経由して、再び、圧縮機21に吸入される。このように、空気調和装置1は、室外熱交換器23を圧縮機21において圧縮される冷媒の凝縮器として、かつ、室内熱交換器42を室外熱交換器23において凝縮された後に第1冷媒連絡管6及び室内膨張弁41を通じて送られる冷媒の蒸発器として機能させる冷房運転を行う。   This low-pressure gas refrigerant is sent to the air-conditioning outdoor unit 2 via the second refrigerant communication pipe 7, and is again sucked into the compressor 21 via the gas-side closing valve 28 b and the switching mechanism 22. As described above, the air conditioner 1 uses the outdoor heat exchanger 23 as a condenser for the refrigerant compressed in the compressor 21, and the indoor heat exchanger 42 is condensed in the outdoor heat exchanger 23 before the first refrigerant. The cooling operation is performed so as to function as an evaporator of the refrigerant sent through the communication pipe 6 and the indoor expansion valve 41.

(3−1−2)異常時の冷房運転
通常時の冷房運転から異常時の冷房運転に切り換わるのは、室内制御装置47において、室内熱交換器42の手前が過冷却状態になっていると判断されたときである。室内制御装置47は、室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも高くなっているとき(Tein>Th2)に、室内熱交換器42の手前が過冷却状態になっていると判断する。
(3-1-2) Cooling operation at the time of abnormality Switching from the cooling operation at the normal time to the cooling operation at the time of abnormality is that the indoor heat exchanger 42 is in an overcooled state in the indoor control device 47. It is when it is judged. When the indoor unit liquid pipe pressure saturation temperature Tein is higher than the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 (Tein> Th2), the indoor controller 47 moves the indoor heat exchanger 42 in front of the indoor heat exchanger 42. Judged to be supercooled.

室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも高くなっている状態とは、図3に示されているような冷凍サイクルで運転されている状態である。つまり、図3において、飽和液線L1が蒸発圧力P2と交わる点AのエンタルピhAよりも室内膨張弁41によって膨張された後の点Bの冷媒のエンタルピhBが低くなっている状態である。このような状態では、室内熱交換器42に流入する冷媒に過冷却度がついているため室内熱交換器42前後の温度差をもとに過熱度制御を行うと、実際の過熱度を誤検知してしまう。その結果、室内熱交換器42の出口で冷媒が二相状態であるにも関わらず過熱状態だと誤認し、室内膨張弁41の開度を多少調節しても二相状態の冷媒の温度は変化せず、制御不能になることがある。   The state where the indoor unit liquid pipe pressure saturation temperature Tein is higher than the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 is a state where the indoor unit liquid pipe pressure saturation temperature Tein is operated in a refrigeration cycle as shown in FIG. is there. That is, in FIG. 3, the enthalpy hB of the refrigerant at the point B after being expanded by the indoor expansion valve 41 is lower than the enthalpy hA at the point A where the saturated liquid line L1 intersects the evaporation pressure P2. In such a state, since the refrigerant flowing into the indoor heat exchanger 42 has a supercooling degree, if the superheat degree control is performed based on the temperature difference between the front and back of the indoor heat exchanger 42, the actual superheat degree is erroneously detected. Resulting in. As a result, even though the refrigerant is in a two-phase state at the outlet of the indoor heat exchanger 42, it is mistakenly regarded as being overheated, and even if the opening degree of the indoor expansion valve 41 is slightly adjusted, the temperature of the refrigerant in the two-phase state is It may not change and become uncontrollable.

そこで、室内制御装置47は、Tein>Th2と判断すると、冷媒の過熱度の目標値を第1過熱度目標値Tsh1から第2過熱度目標値Tsh2に切り換えて室内膨張弁41の開度調節を行う。ここで、第2過熱度目標値Tsh2は、第1過熱度目標値Tsh1よりも大きい(Tsh2>Tsh1)。   Therefore, if the indoor control device 47 determines that Tein> Th2, the indoor superheat valve 41 is adjusted by switching the target value of the superheat degree of the refrigerant from the first superheat degree target value Tsh1 to the second superheat degree target value Tsh2. Do. Here, the second superheat degree target value Tsh2 is larger than the first superheat degree target value Tsh1 (Tsh2> Tsh1).

発生しうる室内熱交換器42入口での過冷却度を評価し、第1過熱度目標値Tsh1よりも高い温度に設定されている第2過熱度目標値Tsh2に変更することで、過熱度制御を行う際の室内熱交換器42の出口の冷媒を確実に過熱冷媒とし、制御性の悪化を防ぐことができるようになる。   The degree of supercooling at the inlet of the indoor heat exchanger 42 that can be generated is evaluated, and the superheat degree control is performed by changing to the second superheat degree target value Tsh2 set to a temperature higher than the first superheat degree target value Tsh1. As a result, the refrigerant at the outlet of the indoor heat exchanger 42 can be reliably used as a superheated refrigerant, thereby preventing deterioration of controllability.

しかし、過熱度の目標値を第2過熱度目標値Tsh2に変更して運転することは、効率の低下につながる。そのため、第1過熱度目標値Tsh1に戻せるような状態になれば、室内制御装置47は、過熱度の目標値を第1過熱度目標値Tsh1に戻す。具体的には、例えば、室内制御装置47は、室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも予め設定されている温度β(数度程度(例えば3℃))だけ低くなっていることが検出された時点で、過熱度の目標値を第2過熱度目標値Tsh2から第1過熱度目標値Tsh1に変更する。つまり、Tein<Th2−βの条件が満たされた時点で過熱度の目標値が切り換えられる。この温度βは、ハンチング防止のためのマージンである。   However, changing the superheat degree target value to the second superheat degree target value Tsh2 leads to a decrease in efficiency. Therefore, if it will be in the state which can be returned to 1st superheat degree target value Tsh1, the indoor control apparatus 47 will return the target value of superheat degree to 1st superheat degree target value Tsh1. Specifically, for example, the indoor control device 47 determines that the indoor unit liquid pipe pressure saturation temperature Tein is set to a temperature β (several degrees (eg, several degrees) that is set in advance from the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44. When it is detected that the temperature is lowered by 3 ° C.), the superheat degree target value is changed from the second superheat degree target value Tsh2 to the first superheat degree target value Tsh1. That is, the target value of the superheat degree is switched when the condition of Tein <Th2-β is satisfied. This temperature β is a margin for preventing hunting.

(3−2)暖房運転
暖房運転時は、切換機構22が図1の破線で示される状態、すなわち、圧縮機21の吐出側がガス側閉鎖弁28b及び第2冷媒連絡管7を介して室内熱交換器42のガス側に接続され、かつ、圧縮機21の吸入側が室外熱交換器23のガス側に接続された状態となっている。室外第1膨張弁25は、室外熱交換器23に流入する冷媒を室外熱交換器23において蒸発させることが可能な圧力(すなわち、蒸発圧力)まで減圧するために開度調節されるようになっている。また、液側閉鎖弁28a及びガス側閉鎖弁28bは、開状態にされている。室内膨張弁41は、室内熱交換器42の出口における冷媒の過冷却度が過冷却度目標値で一定になるように開度調節されるようになっている。室内熱交換器42の出口における冷媒の過冷却度は、吐出圧力センサ31により検出される圧縮機21の吐出圧力が凝縮温度に対応する飽和温度に換算され、この冷媒の飽和温度から室内液管温度センサ44により検出される冷媒温度が差し引かれることによって検出される。
(3-2) Heating Operation During the heating operation, the switching mechanism 22 is in the state indicated by the broken line in FIG. 1, that is, the discharge side of the compressor 21 is heated in the room via the gas-side stop valve 28 b and the second refrigerant communication pipe 7. It is connected to the gas side of the exchanger 42 and the suction side of the compressor 21 is connected to the gas side of the outdoor heat exchanger 23. The opening degree of the outdoor first expansion valve 25 is adjusted in order to reduce the refrigerant flowing into the outdoor heat exchanger 23 to a pressure at which the refrigerant can be evaporated in the outdoor heat exchanger 23 (that is, evaporation pressure). ing. Moreover, the liquid side closing valve 28a and the gas side closing valve 28b are opened. The opening of the indoor expansion valve 41 is adjusted so that the degree of supercooling of the refrigerant at the outlet of the indoor heat exchanger 42 is constant at the target value of the degree of supercooling. The degree of supercooling of the refrigerant at the outlet of the indoor heat exchanger 42 is converted to a saturation temperature corresponding to the condensing temperature of the discharge pressure of the compressor 21 detected by the discharge pressure sensor 31, and from the saturation temperature of the refrigerant to the indoor liquid pipe. It is detected by subtracting the refrigerant temperature detected by the temperature sensor 44.

この冷凍装置10の状態で、圧縮機21、室外ファン26及び室内ファン43を運転すると、低圧のガス冷媒は、圧縮機21に吸入されて圧縮されて高圧のガス冷媒となり、切換機構22、ガス側閉鎖弁28b及び第2冷媒連絡管7を経由して、空調室内機4に送られる。   When the compressor 21, the outdoor fan 26, and the indoor fan 43 are operated in the state of the refrigeration apparatus 10, the low-pressure gas refrigerant is sucked into the compressor 21 and compressed to become a high-pressure gas refrigerant, and the switching mechanism 22, gas The air is sent to the air conditioning indoor unit 4 via the side closing valve 28 b and the second refrigerant communication pipe 7.

そして、空調室内機4に送られた高圧のガス冷媒は、室内熱交換器42において、室内空気と熱交換を行って凝縮して高圧の液冷媒となった後、室内膨張弁41を通過する際に、室内膨張弁41の弁開度に応じて減圧される。   The high-pressure gas refrigerant sent to the air-conditioning indoor unit 4 exchanges heat with indoor air in the indoor heat exchanger 42 to condense into high-pressure liquid refrigerant, and then passes through the indoor expansion valve 41. At this time, the pressure is reduced according to the opening degree of the indoor expansion valve 41.

この室内膨張弁41を通過した冷媒は、第1冷媒連絡管6を経由して空調室外機2に送られ、液側閉鎖弁28a、液ガス熱交換器27及び室外第1膨張弁25を経由してさらに減圧された後に、室外熱交換器23に流入する。そして、室外熱交換器23に流入した低圧の気液二相状態の冷媒は、室外ファン26によって供給される室外空気と熱交換を行って蒸発して低圧のガス冷媒となり、切換機構22を経由して、再び、圧縮機21に吸入される。   The refrigerant that has passed through the indoor expansion valve 41 is sent to the air conditioning outdoor unit 2 via the first refrigerant communication pipe 6, and passes through the liquid side closing valve 28 a, the liquid gas heat exchanger 27, and the outdoor first expansion valve 25. After the pressure is further reduced, it flows into the outdoor heat exchanger 23. The low-pressure gas-liquid two-phase refrigerant flowing into the outdoor heat exchanger 23 exchanges heat with outdoor air supplied by the outdoor fan 26 to evaporate into a low-pressure gas refrigerant, and passes through the switching mechanism 22. Then, it is sucked into the compressor 21 again.

以上のような運転制御は、冷房運転及び暖房運転を含む通常運転を行う空調制御装置8(室内制御装置47と室外制御装置30とこれらの間を接続する伝送線8a)によって行われる。   The operation control as described above is performed by the air conditioning control device 8 (the indoor control device 47 and the outdoor control device 30 and the transmission line 8a connecting them) that performs the normal operation including the cooling operation and the heating operation.

(4)冷凍装置の特徴
(4−1)本実施形態に係る冷凍装置10では、冷房運転時に、圧縮機21と室外熱交換器23(放熱器)と室内熱交換器42(蒸発器)とが順に接続されて冷媒が循環する室内側主冷媒回路10a及び室外側主冷媒回路10c(冷凍回路)が形成されている。室内熱交換器42の流入側に設けられている室内膨張弁41(膨張機構)は、室内熱交換器42の流出側の過熱度目標値に基づいて室内熱交換器42に流入する冷媒の膨張を制御する。室内液管温度センサ44及び吸入圧力センサ33(検出器)により、室内熱交換器42の流入側の冷媒の過冷却状態が検出される。室内制御装置47(制御部)は、室内液管温度センサ44及び吸入圧力センサ33の検出結果に基づいて室内熱交換器42の流入側の冷媒が過冷却状態にあると判断した場合に、過熱度目標値を第1過熱度目標値Tsh1から第2過熱度目標値Tsh2に上げる設定変更を行う。
(4) Features of the refrigeration apparatus (4-1) In the refrigeration apparatus 10 according to the present embodiment, during the cooling operation, the compressor 21, the outdoor heat exchanger 23 (radiator), the indoor heat exchanger 42 (evaporator), Are connected in order, and the indoor main refrigerant circuit 10a and the outdoor main refrigerant circuit 10c (refrigeration circuit) in which the refrigerant circulates are formed. The indoor expansion valve 41 (expansion mechanism) provided on the inflow side of the indoor heat exchanger 42 expands the refrigerant flowing into the indoor heat exchanger 42 based on the superheat degree target value on the outflow side of the indoor heat exchanger 42. To control. The indoor liquid pipe temperature sensor 44 and the suction pressure sensor 33 (detector) detect the supercooled state of the refrigerant on the inflow side of the indoor heat exchanger 42. When the indoor control device 47 (control unit) determines that the refrigerant on the inflow side of the indoor heat exchanger 42 is in a supercooled state based on the detection results of the indoor liquid pipe temperature sensor 44 and the suction pressure sensor 33, The setting change is made to raise the degree target value from the first superheat degree target value Tsh1 to the second superheat degree target value Tsh2.

室内熱交換器42の流入側の冷媒が過冷却状態にあると判断した場合に、過熱度目標値を上げる設定変更を行うので、室内熱交換器42の過熱度制御ができなくなる状況を回避して室内熱交換器42の過熱度の制御を適切に行なわせることができる。そのため、室内熱交換器42の手前で冷媒が過冷却状態になり易い冷凍装置10の過熱度制御を適切に行わせることができる。特に、冷媒量が多いために、蒸発器として機能している室内熱交換器42(利用側熱交換器)の手前で冷媒が過冷却状態になり易い場合に十分な対応が可能になる。   When it is determined that the refrigerant on the inflow side of the indoor heat exchanger 42 is in a supercooled state, the setting change is performed to increase the superheat degree target value, so that a situation in which the superheat degree control of the indoor heat exchanger 42 cannot be performed is avoided. Thus, the degree of superheat of the indoor heat exchanger 42 can be appropriately controlled. Therefore, the superheat degree control of the refrigeration apparatus 10 in which the refrigerant is likely to be in a supercooled state before the indoor heat exchanger 42 can be appropriately performed. In particular, since the amount of the refrigerant is large, it is possible to sufficiently cope with the case where the refrigerant is likely to be supercooled in front of the indoor heat exchanger 42 (use side heat exchanger) functioning as an evaporator.

(4−2)吸入圧力センサ33は、室内熱交換器42(利用側熱交換器)の流入側の圧力飽和温度を検出するための第1検出器であり、室内液管温度センサ44は、室内熱交換器42の流入側の冷媒の温度を検出するための第2検出器である。室内制御装置47(制御部)は、室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも大きいか否か(第1検出器と第2検出器の検出結果の比較)に基づいて、室内熱交換器42の流入側の冷媒が過冷却状態にあるか否かを判断する。そのため、室内熱交換器42の流入側の冷媒に過冷却がついていても、正確に過冷却状態の判断を行なうことができる。   (4-2) The suction pressure sensor 33 is a first detector for detecting the pressure saturation temperature on the inflow side of the indoor heat exchanger 42 (use side heat exchanger), and the indoor liquid pipe temperature sensor 44 is It is a 2nd detector for detecting the temperature of the refrigerant | coolant of the inflow side of the indoor heat exchanger 42. FIG. The indoor control device 47 (control unit) determines whether the indoor unit liquid pipe pressure saturation temperature Tein is higher than the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 (detection by the first detector and the second detector). Based on the comparison of the results, it is determined whether or not the refrigerant on the inflow side of the indoor heat exchanger 42 is in a supercooled state. Therefore, even if the refrigerant on the inflow side of the indoor heat exchanger 42 is supercooled, it is possible to accurately determine the supercooled state.

このように室内熱交換器42(利用側熱交換器)の流入側の冷媒が過冷却状態にあるか否かの判断を行うための第2検出器に、従来からある室内液管温度センサ44を用いることができるので、コストの上昇を抑制できる。同様に、室内熱交換器42の流入側の冷媒が過冷却状態にあるか否かの判断を行うための第1検出器に、従来からある吸入圧力センサ33を用いることができるので、コストの上昇を抑制できる。   Thus, the conventional indoor liquid pipe temperature sensor 44 is used as a second detector for determining whether or not the refrigerant on the inflow side of the indoor heat exchanger 42 (use side heat exchanger) is in a supercooled state. Therefore, an increase in cost can be suppressed. Similarly, the conventional suction pressure sensor 33 can be used as the first detector for determining whether or not the refrigerant on the inflow side of the indoor heat exchanger 42 is in a supercooled state. The rise can be suppressed.

(5)変形例
(5−1)変形例A
上記実施形態の冷凍装置10では、冷房運転時において、室内熱交換器42(蒸発器)が過冷却状態にあると判断されたときに、室内制御装置47が過熱度目標値を上げる場合について説明したが、室内制御装置47で過冷却状態になっていると判断されたときに、室外制御装置30が低圧目標値を下げるように設定を変更してもよい。冷凍装置10の場合、低圧目標値は室内機液管圧力飽和温度Teinである。このような場合には、空調制御装置8が制御部となる。空調制御装置8は、上述のように室内液管温度センサ44と吸入圧力センサ33の検出結果から、低圧目標値を第1低圧目標値PL1からそれよりも低い第2低圧目標値PL2に変更する。つまり、PL1>PL2である。
(5) Modification (5-1) Modification A
In the refrigeration apparatus 10 of the above-described embodiment, the case where the indoor control device 47 increases the superheat degree target value when it is determined that the indoor heat exchanger 42 (evaporator) is in the supercooled state during the cooling operation will be described. However, the setting may be changed so that the outdoor control device 30 decreases the low-pressure target value when it is determined that the indoor control device 47 is in the supercooled state. In the case of the refrigeration apparatus 10, the low pressure target value is the indoor unit liquid pipe pressure saturation temperature Tein. In such a case, the air conditioning control device 8 becomes a control unit. The air-conditioning control device 8 changes the low-pressure target value from the first low-pressure target value PL1 to the second low-pressure target value PL2 lower than the first low-pressure target value PL1 based on the detection results of the indoor liquid pipe temperature sensor 44 and the suction pressure sensor 33 as described above. . That is, PL1> PL2.

低圧目標値が、第1低圧目標値PL1よりも低い第2低圧目標値PL2に変更されると、過熱度目標値が変わらないため、室内膨張弁41における圧力低下が大きくなり、蒸発圧力が低下する。それにより、室内膨張弁41を通過した時点B1での冷媒の状態が、図3に示すように蒸発圧力が例えばP3に低下して室内膨張弁41の下流側(室内熱交換器42の流入側)が気液二相状態に変化し、過熱度による制御が行えるようになる。   When the low pressure target value is changed to the second low pressure target value PL2 that is lower than the first low pressure target value PL1, the superheat degree target value does not change, so the pressure drop in the indoor expansion valve 41 increases and the evaporation pressure decreases. To do. As a result, the state of the refrigerant at the time B1 when it passes through the indoor expansion valve 41 is reduced to e.g. P3 as shown in FIG. 3, and the downstream side of the indoor expansion valve 41 (the inflow side of the indoor heat exchanger 42) ) Changes to a gas-liquid two-phase state, and control based on the degree of superheat becomes possible.

この第2低圧目標値L2に設定された場合、室内制御装置47は、例えば、低圧目標上限値を、室内機液管圧力飽和温度Tein目標値が室内機液管温度Th2に等しいとして運転する。そして、このような条件で運転して、負荷率などの関係で低圧(Tein)が低下する場合には、自動的に上述の判定条件から外れて通常の制御に移行する。つまり、室内制御装置47は、室内機液管圧力飽和温度Teinが室内液管温度センサ44で検出される温度Th2以下であること(Tein≦Th2)を検出し、その検出結果に基づいて低圧目標値を第2低圧目標値PL2から第1低圧目標値PL1に変更する。   When the second low pressure target value L2 is set, the indoor control device 47 operates, for example, assuming that the low pressure target upper limit is equal to the indoor unit liquid pipe pressure saturation temperature Tein target value equal to the indoor unit liquid pipe temperature Th2. When the operation is performed under such conditions and the low pressure (Tein) decreases due to a load factor or the like, the operation automatically shifts from the above-described determination condition to normal control. That is, the indoor control device 47 detects that the indoor unit liquid pipe pressure saturation temperature Tein is equal to or lower than the temperature Th2 detected by the indoor liquid pipe temperature sensor 44 (Tein ≦ Th2), and based on the detection result, the low pressure target. The value is changed from the second low pressure target value PL2 to the first low pressure target value PL1.

(5−2)変形例B
上記実施形態の冷凍装置10では、冷房時において、室内機液管圧力飽和温度Teinが室内液管温度センサ44により検出される冷媒温度Th2よりも高くなっているとき(Tein>Th2)に、室内熱交換器42の流入側が過冷却になっていると判断したが、室外機液管入口温度T1を用いて判断することもできる。室外機液管入口温度T1は、例えば液管温度センサ35(第3検出器)により検出される温度である。室内制御装置47は、熱損失分を考慮して、Tein>T1−αの条件を満たすときに、室内熱交換器42の流入側が過冷却になっていると判断する。そして、室内制御装置47は、この条件を満たしたときに過熱度目標値を第1過熱度目標値Tsh1から第2過熱度目標値Tsh2に変更するか又は低圧目標値を第1低圧目標値PL1から第2低圧目標値PL2に変更する。ただし、αは、熱損失に係る値であって実験などから導かれる値であり、例えば3℃程度である。
(5-2) Modification B
In the refrigeration apparatus 10 of the above embodiment, during cooling, when the indoor unit liquid pipe pressure saturation temperature Tein is higher than the refrigerant temperature Th2 detected by the indoor liquid pipe temperature sensor 44 (Tein> Th2), Although it is determined that the inflow side of the heat exchanger 42 is supercooled, it can also be determined using the outdoor unit liquid pipe inlet temperature T1. The outdoor unit liquid pipe inlet temperature T1 is a temperature detected by, for example, the liquid pipe temperature sensor 35 (third detector). The indoor control device 47 determines that the inflow side of the indoor heat exchanger 42 is supercooled when the condition of Tein> T1-α is satisfied in consideration of the heat loss. Then, the indoor control device 47 changes the superheat degree target value from the first superheat degree target value Tsh1 to the second superheat degree target value Tsh2 when this condition is satisfied, or changes the low pressure target value to the first low pressure target value PL1. To the second low pressure target value PL2. However, (alpha) is a value which concerns on heat loss, and is a value derived | led-out from experiment etc., for example, is about 3 degreeC.

室内熱交換器42の流入側が過冷却になっていると判断されたときに室内制御装置47が行う過熱度目標値の切り換えや低圧目標値の切り換えは、上記実施形態や変形例Bと同様である。   The switching of the superheat degree target value and the switching of the low pressure target value performed by the indoor control device 47 when it is determined that the inflow side of the indoor heat exchanger 42 is undercooling is the same as in the above-described embodiment and modification B. is there.

また、室内熱交換器42の流入側が過冷却の状態から過冷却でない状態に変わって過熱度目標値や低圧目標値を元に戻してもよいか否かの判断も、室外機液管入口温度T1を用いて行われる。つまり、Tein≦T1−α−βという条件を満たすことが検出された時点で、熱温度目標値を第2過熱度目標値Tsh2から第1過熱度目標値Tsh1に変更するか又は低圧目標値を第2低圧目標値PL2から第1低圧目標値PL1に変更する。   In addition, whether the inflow side of the indoor heat exchanger 42 is changed from the supercooling state to the non-supercooling state to return the superheat degree target value or the low pressure target value to the original value is also determined by the outdoor unit liquid pipe inlet temperature. This is done using T1. That is, when it is detected that the condition of Tein ≦ T1-α−β is detected, the thermal temperature target value is changed from the second superheat degree target value Tsh2 to the first superheat degree target value Tsh1, or the low pressure target value is changed. The second low pressure target value PL2 is changed to the first low pressure target value PL1.

このように室内熱交換器42(利用側熱交換器)の流入側の冷媒が過冷却状態にあるか否かの判断を行うための第3検出器に、従来からある液管温度センサ35(熱源側液管温度センサ)を用いることができるので、コストの上昇を抑制できる。同様に、室内熱交換器42の流入側の冷媒が過冷却状態にあるか否かの判断を行うための第1検出器に、従来からある吸入圧力センサ33を用いることができるので、コストの上昇を抑制できる。   Thus, the conventional liquid tube temperature sensor 35 (in the third detector for determining whether or not the refrigerant on the inflow side of the indoor heat exchanger 42 (use side heat exchanger) is in a supercooled state is used. Since a heat source side liquid pipe temperature sensor) can be used, an increase in cost can be suppressed. Similarly, the conventional suction pressure sensor 33 can be used as the first detector for determining whether or not the refrigerant on the inflow side of the indoor heat exchanger 42 is in a supercooled state. The rise can be suppressed.

(5−3)変形例C
上記の実施形態及び上記の変形例Aでは、冷房運転時に、室内熱交換器42が蒸発器として機能する場合について説明したが、暖房運転時に室外熱交換器23の流入側の冷媒が過冷却状態になりやすい場合にも本願発明を適用できる。
(5-3) Modification C
In the above embodiment and the above modification A, the case where the indoor heat exchanger 42 functions as an evaporator during the cooling operation has been described. However, the refrigerant on the inflow side of the outdoor heat exchanger 23 is in a supercooled state during the heating operation. The present invention can also be applied to cases where it is likely to occur.

室外熱交換器23の流入側で過冷却状態が生じているかいなかは、上述の低圧Teinと室外機液管入口温度T1とを用いて、Tein>T1−αの条件を満たすようになっているか否かを検出することにより室外制御装置30において判断することができる。   Whether or not a supercooling state has occurred on the inflow side of the outdoor heat exchanger 23 is whether the condition of Tein> T1-α is satisfied using the low-pressure Tein and the outdoor unit liquid pipe inlet temperature T1 described above. It can be judged in the outdoor control device 30 by detecting whether or not.

暖房運転時には、高圧目標値が設定されているため、室外熱交換器23の流入側で過冷却状態が生じていると判断されたときには、高圧目標値を第1高圧目標値HP1から第2高圧目標値HP2に変更する。この場合、第1高圧目標値HP1よりも第2高圧目標値HP2が高く設定されている(HP2>HP1)。   Since the high pressure target value is set during the heating operation, when it is determined that a supercooling state has occurred on the inflow side of the outdoor heat exchanger 23, the high pressure target value is changed from the first high pressure target value HP1 to the second high pressure target value. Change to the target value HP2. In this case, the second high pressure target value HP2 is set higher than the first high pressure target value HP1 (HP2> HP1).

そして、上記実施形態や変形例A,Bと同様に、Tein≦T1−α−βの条件を満たすようになっていることを検出すると、高圧目標値を通常の状態に戻す。つまり、室外熱交換器23の流入側で過冷却状態が解消されたと判断されたときには、高圧目標値を第2高圧目標値HP2から第1高圧目標値HP1に変更する。   And if it detects that the conditions of Tein <= T1- (alpha)-(beta) are satisfy | filled similarly to the said embodiment and modification A, B, a high voltage | pressure target value will be returned to a normal state. That is, when it is determined that the supercooling state has been eliminated on the inflow side of the outdoor heat exchanger 23, the high pressure target value is changed from the second high pressure target value HP2 to the first high pressure target value HP1.

(5−4)変形例D
上記実施形態では、空調室内機4の構成として、同じ空調室内機4a,4bが2台接続されている場合について説明したが、1台又は3台以上の空調室内機が接続されてもよい。また、複数台の空調室内機が接続される場合には、異なる構成の空調室内機が接続されてもよい。
(5-4) Modification D
Although the said embodiment demonstrated the case where two same air-conditioning indoor units 4a and 4b were connected as a structure of the air-conditioning indoor unit 4, 1 unit | set or 3 or more air-conditioning indoor units may be connected. When a plurality of air conditioning indoor units are connected, air conditioning indoor units having different configurations may be connected.

(5−5)変形例E
上記実施形態では、過熱度目標値を第1過熱度目標値Tsh1よりも高い温度に設定されている第2過熱度目標値Tsh2に変更する場合について説明した。しかし、第2過熱度目標値として、複数の異なる過熱度目標値を設定することもできる。例えば、第2過熱度目標値Tsh2よりも高い第3過熱度目標値Tsh3を設け、過冷却度Tscが0<Tsc≦Tsc1の条件を満たすときは第2過熱度目標値Tsh2を用い、過冷却度TscがTsc1<Tscの条件を満たすときは第3過熱度目標値Tsh3を用いるように構成することもできる。また、予め第2過熱度目標値Tsh2と過冷却度Tscとの関係式を準備しておき、室内熱交換器42入口での過冷却度を評価し、過冷却度の程度に応じて第2過熱度目標値Tsh2を第1過熱度目標値Tsh1よりも高い温度にするように変更することもできる。なお、第2過熱度目標値Tsh2と過冷却度Tscとの関係式は、例えば予め行う実験や試運転など通じて適宜決定すればよい。
(5-5) Modification E
In the above embodiment, the case where the superheat degree target value is changed to the second superheat degree target value Tsh2 set to a temperature higher than the first superheat degree target value Tsh1 has been described. However, a plurality of different superheat degree target values can be set as the second superheat degree target value. For example, when the third superheat degree target value Tsh3 higher than the second superheat degree target value Tsh2 is provided and the degree of supercooling Tsc satisfies the condition 0 <Tsc ≦ Tsc1, the second superheat degree target value Tsh2 is used to perform the supercooling. When the degree Tsc satisfies the condition of Tsc1 <Tsc, the third superheat degree target value Tsh3 may be used. In addition, a relational expression between the second superheat degree target value Tsh2 and the supercooling degree Tsc is prepared in advance, the supercooling degree at the inlet of the indoor heat exchanger 42 is evaluated, and the second superheating degree is calculated according to the degree of the supercooling degree. The superheat degree target value Tsh2 can be changed to a temperature higher than the first superheat degree target value Tsh1. Note that the relational expression between the second superheat degree target value Tsh2 and the supercooling degree Tsc may be determined as appropriate through, for example, an experiment or trial operation that is performed in advance.

10 冷凍装置
21 圧縮機
23 室外熱交換器
30 室外制御装置
32 吐出温度センサ
33 吸入圧力センサ
41 室内膨張弁
42 室内熱交換器
44 室内液管温度センサ
47 室内制御装置
DESCRIPTION OF SYMBOLS 10 Refrigeration apparatus 21 Compressor 23 Outdoor heat exchanger 30 Outdoor control apparatus 32 Discharge temperature sensor 33 Suction pressure sensor 41 Indoor expansion valve 42 Indoor heat exchanger 44 Indoor liquid pipe temperature sensor 47 Indoor control apparatus

特開2004−271066号公報Japanese Patent Laid-Open No. 2004-271066

Claims (7)

圧縮機(21)と放熱器(23,42)と蒸発器(42,23)とが順に接続されて冷媒が循環する冷媒回路が形成されている冷凍装置(10)であって、
前記蒸発器の流入側に設けられ、前記冷媒回路の高圧目標値、前記冷媒回路の低圧目標値及び前記蒸発器の流出側の過熱度目標値のうちの少なくとも一つに基づいて前記蒸発器に流入する冷媒の膨張を制御するための膨張機構(41)と、
前記蒸発器の流入側の冷媒の過冷却状態を検出するための検出器(29,44,35,31)と、
前記検出器の検出結果に基づいて前記蒸発器の流入側の冷媒が過冷却状態にあると判断した場合に、前記高圧目標値を上げる設定変更、前記低圧目標値を下げる設定変更及び前記過熱度目標値を上げる設定変更のうちの少なくとも一つの所定の設定変更を行い得る制御部(47,30,8)と、
を備える、冷凍装置。
A compressor (21), a radiator (23, 42), and an evaporator (42, 23) are connected in order to form a refrigerant circuit (10) in which a refrigerant circuit for circulating refrigerant is formed,
The evaporator is provided on the inflow side of the evaporator, and is supplied to the evaporator based on at least one of a high pressure target value of the refrigerant circuit, a low pressure target value of the refrigerant circuit, and a superheat degree target value on the outflow side of the evaporator. An expansion mechanism (41) for controlling expansion of the refrigerant flowing in;
Detectors (29, 44, 35, 31) for detecting the supercooling state of the refrigerant on the inflow side of the evaporator;
When it is determined that the refrigerant on the inflow side of the evaporator is in a supercooled state based on the detection result of the detector, a setting change that increases the high pressure target value, a setting change that decreases the low pressure target value, and the degree of superheat A control unit (47, 30, 8) capable of performing at least one predetermined setting change among setting changes for increasing the target value;
A refrigeration apparatus comprising:
前記制御部は、前記所定の設定変更を行なった後に、過冷却状態が解消したときには、前記所定の設定変更を元に戻す、  When the supercooling state is resolved after performing the predetermined setting change, the control unit restores the predetermined setting change.
請求項1に記載の冷凍装置。The refrigeration apparatus according to claim 1.
前記制御部は、前記所定の設定変更を行う場合の過冷却状態になったと判断するときの値と前記所定の設定変更を元に戻す場合の過冷却状態を脱したと判断するときの値との間に、ハンチング防止のためのマージンを設けている、  The control unit determines a value when it is determined that the supercooling state is reached when the predetermined setting change is performed, and a value when it is determined that the supercooling state is canceled when the predetermined setting change is restored. A margin for preventing hunting is provided between
請求項2に記載の冷凍装置。The refrigeration apparatus according to claim 2.
前記蒸発器は、利用側熱交換器(42)であり、
前記制御部(47)は、前記検出器の検出結果に基づいて前記利用側熱交換器の流入側の冷媒が過冷却状態にあると判断した場合に、前記低圧目標値を下げる設定変更及び前記過熱度目標値を上げる設定変更のうちの少なくとも一方を行い得る、
請求項1から3のいずれか一項に記載の冷凍装置。
The evaporator is a use side heat exchanger (42),
When the control unit (47) determines that the refrigerant on the inflow side of the use-side heat exchanger is in a supercooled state based on the detection result of the detector, the setting change to lower the low-pressure target value and the Can perform at least one of setting changes to increase the superheat target value,
The refrigeration apparatus according to any one of claims 1 to 3 .
前記検出器は、前記利用側熱交換器の流入側の圧力飽和温度を検出するための第1検出器(33)と前記利用側熱交換器の流入側の冷媒の温度を検出するための第2検出器(44)、又は前記第1検出器(33)と前記膨張機構の流入側の冷媒の温度を検出するための第3検出器(35)を含み、
前記制御部は、前記第1検出器と前記第2検出器の検出結果の比較又は前記第1検出器と前記第3検出器の検出結果の比較に基づいて、前記利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かを判断し得る、
請求項に記載の冷凍装置。
The detector includes a first detector (33) for detecting the pressure saturation temperature on the inflow side of the use side heat exchanger and a first detector for detecting the temperature of the refrigerant on the inflow side of the use side heat exchanger. 2 detector (44), or a first detector (33) and a third detector (35) for detecting the temperature of the refrigerant on the inflow side of the expansion mechanism,
The control unit is configured to inflow the user-side heat exchanger based on a comparison of detection results of the first detector and the second detector or a comparison of detection results of the first detector and the third detector. It can be determined whether the refrigerant on the side is in a supercooled state,
The refrigeration apparatus according to claim 4 .
前記第3検出器は、前記放熱器の流出側に設けられている液管温度センサ(35)であり、
前記制御部は、前記液管温度センサの取り付け位置から前記膨張機構までの熱損失に相当する補正値を前記液管温度センサの検出温度より差し引いて得られる温度を前記膨張機構の流入側の冷媒の温度として用いて前記利用側熱交換器の流入側の冷媒が過冷却状態にあるか否かを判断し得る、
請求項5に記載の冷凍装置。
The third detector is a liquid pipe temperature sensor (35) provided on the outflow side of the radiator,
The controller is configured to subtract a correction value corresponding to a heat loss from the attachment position of the liquid pipe temperature sensor to the expansion mechanism from a temperature detected by the liquid pipe temperature sensor, and to obtain a refrigerant on the inflow side of the expansion mechanism. It can be determined whether or not the refrigerant on the inflow side of the use side heat exchanger is in a supercooled state using as the temperature of
The refrigeration apparatus according to claim 5 .
前記第1検出器は、前記圧縮機の吸入側の圧力を検知する吸入圧力センサ(33)であり、
前記制御部は、前記吸入圧力センサによって検出される圧力から前記圧力飽和温度を算出し得る、
請求項又は請求項に記載の冷凍装置。
The first detector is a suction pressure sensor (33) for detecting the pressure on the suction side of the compressor,
The control unit can calculate the pressure saturation temperature from the pressure detected by the suction pressure sensor,
The refrigeration apparatus according to claim 5 or 6 .
JP2011290079A 2011-12-28 2011-12-28 Refrigeration equipment Active JP5447499B2 (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
JP2011290079A JP5447499B2 (en) 2011-12-28 2011-12-28 Refrigeration equipment
EP12862685.0A EP2806233B1 (en) 2011-12-28 2012-12-26 Refrigeration device
KR1020147020685A KR101479458B1 (en) 2011-12-28 2012-12-26 Refrigeration device
BR112014015866A BR112014015866A8 (en) 2011-12-28 2012-12-26 cooling appliance
PCT/JP2012/083565 WO2013099898A1 (en) 2011-12-28 2012-12-26 Refrigeration device
ES12862685T ES2861271T3 (en) 2011-12-28 2012-12-26 Cooling device
CN201280064456.3A CN104024764B (en) 2011-12-28 2012-12-26 Refrigeration apparatus
US14/368,704 US20140373564A1 (en) 2011-12-28 2012-12-26 Refrigeration apparatus
AU2012361734A AU2012361734B2 (en) 2011-12-28 2012-12-26 Refrigeration apparatus
AU2016202855A AU2016202855B2 (en) 2011-12-28 2016-05-04 Refrigeration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011290079A JP5447499B2 (en) 2011-12-28 2011-12-28 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JP2013139924A JP2013139924A (en) 2013-07-18
JP5447499B2 true JP5447499B2 (en) 2014-03-19

Family

ID=48697382

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011290079A Active JP5447499B2 (en) 2011-12-28 2011-12-28 Refrigeration equipment

Country Status (9)

Country Link
US (1) US20140373564A1 (en)
EP (1) EP2806233B1 (en)
JP (1) JP5447499B2 (en)
KR (1) KR101479458B1 (en)
CN (1) CN104024764B (en)
AU (2) AU2012361734B2 (en)
BR (1) BR112014015866A8 (en)
ES (1) ES2861271T3 (en)
WO (1) WO2013099898A1 (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014190554A (en) * 2013-03-26 2014-10-06 Fujitsu General Ltd Air conditioner
JP5900472B2 (en) * 2013-12-03 2016-04-06 ダイキン工業株式会社 Refrigeration apparatus and control method of refrigeration apparatus
JP6169003B2 (en) * 2014-01-14 2017-07-26 三菱電機株式会社 Refrigeration equipment
CN104976711A (en) * 2014-04-14 2015-10-14 大金工业株式会社 Refrigerating device
JP6359423B2 (en) * 2014-10-24 2018-07-18 三菱重工業株式会社 Control device for air conditioning system, air conditioning system, and abnormality determination method for control device for air conditioning system
US10563877B2 (en) * 2015-04-30 2020-02-18 Daikin Industries, Ltd. Air conditioner
CN104896675B (en) * 2015-06-12 2017-12-08 广东美的暖通设备有限公司 The return-air degree of superheat method of testing and multiple on-line system of multiple on-line system
JP6657613B2 (en) * 2015-06-18 2020-03-04 ダイキン工業株式会社 Air conditioner
US20170016659A1 (en) * 2015-07-14 2017-01-19 Nortek Global Hvac Llc Refrigerant charge and control method for heat pump systems
EP3196569A1 (en) * 2016-01-21 2017-07-26 Vaillant GmbH Sensor arramgement in a heat pump system
WO2018078729A1 (en) * 2016-10-25 2018-05-03 三菱電機株式会社 Refrigeration cycle device
WO2018167961A1 (en) * 2017-03-17 2018-09-20 三菱電機株式会社 Air conditioner
CN107559953B (en) * 2017-08-15 2020-02-04 广东美的暖通设备有限公司 Multi-split air conditioning system and control method and device of supercooling loop valve body thereof
CN108759008B (en) * 2018-06-12 2020-09-04 广东美的暖通设备有限公司 Control method and device of air conditioner and air conditioner with control device
WO2020101176A1 (en) * 2018-11-15 2020-05-22 이동원 Heat pump having improved efficiency
PL4134610T3 (en) 2020-08-26 2025-07-14 Gd Midea Heating & Ventilating Equipment Co., Ltd. Air conditioning system
CN214666271U (en) * 2020-08-26 2021-11-09 广东美的暖通设备有限公司 Heat exchanger, electric control box and air conditioning system
CN112556259B (en) * 2020-12-14 2021-11-30 珠海格力电器股份有限公司 Pressure regulation control method and device and air conditioner
DE112023000554T5 (en) * 2022-01-10 2024-11-28 Wellsense, Inc. PRESSURE SENSOR MATS

Family Cites Families (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4697431A (en) * 1984-08-08 1987-10-06 Alsenz Richard H Refrigeration system having periodic flush cycles
US4651535A (en) * 1984-08-08 1987-03-24 Alsenz Richard H Pulse controlled solenoid valve
US5222371A (en) * 1989-12-28 1993-06-29 Matsushita Electric Industrial Co., Ltd. Air conditioner of multichamber type
US5187944A (en) * 1992-04-10 1993-02-23 Eaton Corporation Variable superheat target strategy for controlling an electrically operated refrigerant expansion valve
US5551248A (en) * 1995-02-03 1996-09-03 Heatcraft Inc. Control apparatus for space cooling system
SG98373A1 (en) * 1998-11-25 2003-09-19 Advantest Corp Device testing apparatus
US6044651A (en) * 1999-03-26 2000-04-04 Carrier Corporation Economy mode for transport refrigeration units
CA2341316A1 (en) * 2000-03-17 2001-09-17 Samir Kuliev Digital indirectly compensated crystal oscillators
JP4259891B2 (en) 2003-03-10 2009-04-30 株式会社テージーケー Superheat control method
JP2004301456A (en) * 2003-03-31 2004-10-28 Toyota Industries Corp Refrigerating cycle apparatus and equipment for the same
JP4367176B2 (en) * 2003-05-16 2009-11-18 株式会社デンソー Exhaust gas purification device for internal combustion engine
US20060112702A1 (en) * 2004-05-18 2006-06-01 George Martin Energy efficient capacity control for an air conditioning system
US7275377B2 (en) * 2004-08-11 2007-10-02 Lawrence Kates Method and apparatus for monitoring refrigerant-cycle systems
US8096141B2 (en) * 2005-01-25 2012-01-17 Trane International Inc. Superheat control by pressure ratio
JP2008520943A (en) * 2005-06-03 2008-06-19 キャリア コーポレイション Heat pump system with auxiliary water heating
US7628027B2 (en) * 2005-07-19 2009-12-08 Hussmann Corporation Refrigeration system with mechanical subcooling
JP4114691B2 (en) * 2005-12-16 2008-07-09 ダイキン工業株式会社 Air conditioner
JP4715561B2 (en) * 2006-03-06 2011-07-06 ダイキン工業株式会社 Refrigeration equipment
JP2009008063A (en) * 2007-06-29 2009-01-15 Calsonic Kansei Corp Control device of variable displacement compressor
CN101784796B (en) * 2007-08-17 2013-03-20 三电有限公司 System for controlling capacity of variable capacity compressor and display device
WO2009103472A1 (en) * 2008-02-20 2009-08-27 Carrier Corporation Method of controlling a heat-rejection heat exchanging side of a refrigerant circuit
JP5326488B2 (en) * 2008-02-29 2013-10-30 ダイキン工業株式会社 Air conditioner
JP5120056B2 (en) * 2008-05-02 2013-01-16 ダイキン工業株式会社 Refrigeration equipment
EP2314953B1 (en) * 2008-06-13 2018-06-27 Mitsubishi Electric Corporation Refrigeration cycle device and control method therefor
JP2010007995A (en) * 2008-06-27 2010-01-14 Daikin Ind Ltd Refrigerant amount determining method of air conditioning device, and air conditioning device
JP2010255884A (en) * 2009-04-22 2010-11-11 Mitsubishi Heavy Ind Ltd Heat source machine and method of controlling the same
WO2010137120A1 (en) * 2009-05-26 2010-12-02 三菱電機株式会社 Heat pump type hot water supply device
JP5233960B2 (en) * 2009-11-06 2013-07-10 パナソニック株式会社 Refrigeration cycle apparatus and hot water heater using the same
JP5502459B2 (en) * 2009-12-25 2014-05-28 三洋電機株式会社 Refrigeration equipment
JP2011179697A (en) * 2010-02-26 2011-09-15 Panasonic Corp Refrigerating cycle device and water heating/cooling device
JP2011185507A (en) * 2010-03-08 2011-09-22 Panasonic Corp Refrigerating cycle device and hot water heating device including the same
EP2565555B1 (en) * 2010-04-27 2021-04-21 Mitsubishi Electric Corporation Refrigeration cycle apparatus
US10018389B2 (en) * 2011-12-22 2018-07-10 Mitsubishi Electric Corporation Air-conditioning apparatus

Also Published As

Publication number Publication date
BR112014015866A8 (en) 2017-07-04
AU2012361734A1 (en) 2014-08-07
JP2013139924A (en) 2013-07-18
AU2016202855B2 (en) 2017-10-26
EP2806233B1 (en) 2021-03-10
CN104024764A (en) 2014-09-03
BR112014015866A2 (en) 2017-06-13
CN104024764B (en) 2015-05-20
KR20140103352A (en) 2014-08-26
US20140373564A1 (en) 2014-12-25
WO2013099898A1 (en) 2013-07-04
ES2861271T3 (en) 2021-10-06
AU2012361734B2 (en) 2016-02-04
KR101479458B1 (en) 2015-01-05
EP2806233A4 (en) 2016-04-13
AU2016202855A1 (en) 2016-05-26
EP2806233A1 (en) 2014-11-26

Similar Documents

Publication Publication Date Title
JP5447499B2 (en) Refrigeration equipment
JP6257801B2 (en) Refrigeration cycle apparatus and refrigeration cycle apparatus abnormality detection system
JP4968373B2 (en) Air conditioner
CN103119377B (en) Refrigeration hot water supply apparatus and refrigeration hot water supply method
CN104567135B (en) Air-conditioning device
JP5979112B2 (en) Refrigeration equipment
JP2018004216A (en) Air conditioner
JP2017075760A (en) Air conditioner
CN107709887A (en) Conditioner and operating control device
JP5966327B2 (en) Air conditioning indoor unit
JP5245576B2 (en) Refrigerant amount determination method for air conditioner and air conditioner
JP5708421B2 (en) Refrigeration equipment
JP6537629B2 (en) Air conditioner
JP6111692B2 (en) Refrigeration equipment
JP5884422B2 (en) Refrigeration equipment

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130530

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

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20131203

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20131216

R151 Written notification of patent or utility model registration

Ref document number: 5447499

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151