JP2008241072A - Refrigerating cycle device - Google Patents

Refrigerating cycle device Download PDF

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JP2008241072A
JP2008241072A JP2007079079A JP2007079079A JP2008241072A JP 2008241072 A JP2008241072 A JP 2008241072A JP 2007079079 A JP2007079079 A JP 2007079079A JP 2007079079 A JP2007079079 A JP 2007079079A JP 2008241072 A JP2008241072 A JP 2008241072A
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refrigerant
valve
expansion valve
cycle apparatus
refrigeration cycle
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JP4983330B2 (en
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Masayoshi Obayashi
誠善 大林
Takashi Okazaki
多佳志 岡崎
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Mitsubishi Electric Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • 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
    • F25B2700/197Pressures 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
    • F25B2700/2106Temperatures of fresh outdoor air

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  • Air Conditioning Control Device (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a refrigerating cycle device capable of quickly charging a refrigerant when the refrigerant is discharged and then recharged. <P>SOLUTION: This refrigerating cycle device comprising a circulation circuit comprising a compressor 110 for compressing and discharging the refrigerant flowing therein, a condenser 120 for condensing the refrigerant discharged from the compressor 110, an expansion valve 130 for expanding the refrigerant from the condenser 120, and an evaporator 140 for evaporating the refrigerant from the expansion valve 130 and allowing the refrigerant to flow into the compressor 110, further comprises an opening and closing valve 160 disposed between the evaporator 140 and the compressor 110 for connecting the circulation circuit and the external, and a control circuit 170 for controlling an opening of the expansion valve 130 when the opening and closing valve 160 is opened. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、冷媒循環回路と、冷媒循環回路から冷媒を排出したり冷媒循環回路に冷媒を封入したりする開閉弁とを備えた冷凍サイクル装置に関するものである。   The present invention relates to a refrigeration cycle apparatus including a refrigerant circulation circuit and an on-off valve that discharges the refrigerant from the refrigerant circulation circuit or encloses the refrigerant in the refrigerant circulation circuit.

近年、脱フロン化の流れを受けて、自然冷媒を用いた冷凍サイクル装置の開発が盛んに進められている。冷凍サイクル装置の適用先は、家庭用給湯を目的としたヒートポンプ式給湯器の他、カーエアコン、空気調和装置、冷凍機、冷蔵庫等である。自然冷媒を用いた冷凍サイクル装置として、特に二酸化炭素を冷媒として用いた冷凍サイクル装置が普及しつつある。二酸化炭素は、オゾン破壊係数が0、地球温暖化係数が1という特性を備え、冷媒として用いれば環境への負荷を小さくできるという利点を有する。また、二酸化炭素は、毒性も可燃性も無いという点で安全性に優れているばかりか、入手が容易であり、比較的安価であるという利点も有している。   In recent years, refrigeration cycle apparatuses using natural refrigerants have been actively developed in response to the flow of defluorination. The application destination of the refrigeration cycle apparatus is a car air conditioner, an air conditioner, a refrigerator, a refrigerator, and the like in addition to a heat pump type water heater intended for domestic hot water supply. As a refrigeration cycle apparatus using a natural refrigerant, a refrigeration cycle apparatus using carbon dioxide as a refrigerant is becoming widespread. Carbon dioxide has the characteristics that the ozone depletion coefficient is 0 and the global warming coefficient is 1, and if it is used as a refrigerant, it has the advantage that the burden on the environment can be reduced. Carbon dioxide is not only excellent in safety in that it is neither toxic nor flammable, but also has the advantage of being readily available and relatively inexpensive.

ところで、二酸化炭素の臨界温度は31.1℃であり、フロンガスと比較すると低い温度で超臨界状態になる。そのため、冷凍サイクル装置の周囲温度(以下、「周囲温度」と称する)が二酸化炭素の臨界温度よりも高くなる場合が頻繁に発生することが考えられる。   By the way, the critical temperature of carbon dioxide is 31.1 ° C., and it becomes a supercritical state at a lower temperature than that of Freon gas. Therefore, it is considered that the case where the ambient temperature of the refrigeration cycle apparatus (hereinafter referred to as “ambient temperature”) is higher than the critical temperature of carbon dioxide frequently occurs.

ここで、冷凍サイクル装置に冷媒を再封入する場合を考える。
家庭用の冷凍サイクル装置が故障した場合、故障した装置を製造業者へ持ち込んで修理や交換をすることが容易に行える。一方、業務用冷凍サイクル装置が故障した場合には、業務停止という二次的被害が発生するので、二次的被害の拡大を防止するために、故障に対する迅速な対応が求められる。しかし、業務用の冷凍サイクル装置は、家庭用の冷凍冷凍サイクル装置よりも重量やサイズが大きいため、故障時に装置を製造業者に持ち込むことが難しい。このため、業務用冷凍サイクル装置の故障発生時には、冷凍サイクル装置が設置された場所で修理や部品交換を行うことが必要となる。
特許文献1には、冷凍サイクル装置の圧力に基づいて冷媒の充填量を調整するという冷媒充填方法および冷媒充填装置が記載されている。冷凍サイクル装置を製造業者に持ち込んだ場合には、このような冷媒充填方法を採用できるものの、冷凍サイクル装置が設置された場所で行うには、そのような冷媒充填のための装置を運搬したり、装置を冷凍サイクル装置に取り付けたりする必要があり、作業の規模が大きくなる。
Here, a case where the refrigerant is re-enclosed in the refrigeration cycle apparatus is considered.
When a household refrigeration cycle device fails, it can be easily repaired or replaced by bringing the failed device to the manufacturer. On the other hand, when a commercial refrigeration cycle apparatus breaks down, a secondary damage such as a business stop occurs, so that a quick response to the failure is required to prevent the secondary damage from spreading. However, since the commercial refrigeration cycle apparatus is larger in weight and size than the domestic refrigeration cycle apparatus, it is difficult to bring the apparatus into the manufacturer at the time of failure. For this reason, when a failure occurs in the commercial refrigeration cycle apparatus, it is necessary to repair or replace parts at the place where the refrigeration cycle apparatus is installed.
Patent Document 1 describes a refrigerant charging method and a refrigerant charging apparatus in which the charging amount of the refrigerant is adjusted based on the pressure of the refrigeration cycle apparatus. When a refrigeration cycle apparatus is brought into a manufacturer, such a refrigerant charging method can be adopted. However, in order to carry out at a place where the refrigeration cycle apparatus is installed, such a refrigerant charging apparatus is transported. It is necessary to attach the apparatus to the refrigeration cycle apparatus, and the scale of work increases.

特開2001−74342JP 2001-74342 A

冷凍サイクル装置が設置された場所で修理や部品交換を行う場合、最初に排出弁から冷媒を排出する工程が発生する。その後、修理や部品交換を行い、真空引きを行い、最後に冷媒を封入する工程が発生する。一般的に、冷媒排出から封入までの作業中、圧縮機は停止している。
また、新たに封入される冷媒は、ボンベに充填され、冷凍サイクル装置が設置された場所まで運搬される。作業者がこのボンベを排出弁に接続して、排出弁およびボンベの弁を開けば、ボンベから冷凍サイクル装置に冷媒が流入する。
When repair or replacement of parts is performed at a place where the refrigeration cycle apparatus is installed, a process of discharging the refrigerant from the discharge valve first occurs. Thereafter, repairs and parts replacement are performed, vacuuming is performed, and finally a step of filling the refrigerant occurs. In general, the compressor is stopped during operations from refrigerant discharge to encapsulation.
Moreover, the newly filled refrigerant is filled in a cylinder and transported to a place where the refrigeration cycle apparatus is installed. When an operator connects the cylinder to the discharge valve and opens the discharge valve and the cylinder valve, the refrigerant flows from the cylinder into the refrigeration cycle apparatus.

次に、冷凍サイクル装置に封入される冷媒が二酸化炭素冷媒であり、一回のボンベ接続で封入できる冷媒量について説明する。
図15は、従来の冷凍サイクル装置において二酸化炭素冷媒を封入する場合の二酸化炭素冷媒の状態変化を示す図である。図15(a)は、ボンベ内および冷凍サイクル装置内の二酸化炭素冷媒の状態変化を示す図であり、図15(b)は図15(a)の大気圧付近を拡大して示した図である。図15(a)、(b)のいずれにおいても、横軸はエンタルピー、縦軸は絶対圧力を示す。図15(a)、(b)において、実線はボンベ内の二酸化炭素冷媒の状態変化を示し、破線は冷凍サイクル装置内の二酸化炭素冷媒の状態変化を示す。ここでは、周囲温度が40℃、ボンベの体積を9L、初期の二酸化炭素の充填量を7.0Kgとする。このときの圧力は14.7MPaである。また、冷凍サイクル装置の内容積を30Lとする。周囲温度が二酸化炭素の臨界温度よりも高いため、ボンベ内の二酸化炭素冷媒は超臨界状態になっている。
Next, the refrigerant sealed in the refrigeration cycle apparatus is a carbon dioxide refrigerant, and the amount of refrigerant that can be sealed with a single cylinder connection will be described.
FIG. 15 is a diagram illustrating a state change of the carbon dioxide refrigerant when the carbon dioxide refrigerant is sealed in the conventional refrigeration cycle apparatus. FIG. 15A is a diagram showing changes in the state of carbon dioxide refrigerant in the cylinder and the refrigeration cycle apparatus, and FIG. 15B is an enlarged view of the vicinity of the atmospheric pressure in FIG. 15A. is there. 15A and 15B, the horizontal axis represents enthalpy and the vertical axis represents absolute pressure. 15 (a) and 15 (b), the solid line indicates the change in the state of the carbon dioxide refrigerant in the cylinder, and the broken line indicates the change in the state of the carbon dioxide refrigerant in the refrigeration cycle apparatus. Here, the ambient temperature is 40 ° C., the cylinder volume is 9 L, and the initial carbon dioxide filling amount is 7.0 kg. The pressure at this time is 14.7 MPa. The internal volume of the refrigeration cycle apparatus is 30L. Since the ambient temperature is higher than the critical temperature of carbon dioxide, the carbon dioxide refrigerant in the cylinder is in a supercritical state.

図15(a)の実線が示すように、ボンベ内の二酸化炭素冷媒の初期状態を状態aとする。ボンベと冷凍サイクル装置とを接続すると、ボンベ内の二酸化炭素冷媒は、温度については周囲温度と同一である状態を維持したままで、冷媒密度および圧力は低下して、最終的に状態bに至る。
一方、図15(a)、(b)の破線が示すように、冷凍サイクル装置内の二酸化炭素冷媒の初期状態を状態cとする。冷凍サイクル装置内の二酸化炭素冷媒も、温度については周囲温度と同一である状態を維持したままで、冷媒密度および圧力は上昇して、ボンベ内の圧力と同等になるまで変化し、最終的に状態bに至る。
ボンベ内および冷凍サイクル装置内の二酸化炭素冷媒の圧力は、最終状態bにおいては約6.7Mpaとなる。また、ボンベから冷凍サイクル装置へ移動した二酸化炭素冷媒の量は5.38Kgであり、1.62Kgはボンベ内に残留する。
As indicated by the solid line in FIG. 15A, the initial state of the carbon dioxide refrigerant in the cylinder is referred to as state a. When the cylinder and the refrigeration cycle apparatus are connected, the carbon dioxide refrigerant in the cylinder remains in a state where the temperature is the same as the ambient temperature, the refrigerant density and pressure decrease, and finally the state b is reached. .
On the other hand, as indicated by the broken lines in FIGS. 15A and 15B, the initial state of the carbon dioxide refrigerant in the refrigeration cycle apparatus is referred to as state c. The carbon dioxide refrigerant in the refrigeration cycle apparatus also remains at the same temperature as the ambient temperature, and the refrigerant density and pressure rise until it becomes equal to the pressure in the cylinder. State b is reached.
The pressure of the carbon dioxide refrigerant in the cylinder and in the refrigeration cycle apparatus is about 6.7 Mpa in the final state b. Further, the amount of carbon dioxide refrigerant transferred from the cylinder to the refrigeration cycle apparatus is 5.38 Kg, and 1.62 Kg remains in the cylinder.

上述の場合は、二酸化炭素冷媒は超臨界状態であるため、冷媒封入時の冷凍サイクル装置内の圧力はすぐに上昇するとともに、ボンベ内の圧力は極度に低下する。このため、一回のボンベ接続では二酸化炭素冷媒を冷凍サイクル装置に十分に封入できず、冷凍サイクル装置に必要な二酸化炭素を充填するために、満充填のボンベを複数回接続しなければならず、作業量が増えるだけでなく、二酸化炭素冷媒を十分充填するまでに時間が掛かる。   In the above-described case, since the carbon dioxide refrigerant is in a supercritical state, the pressure in the refrigeration cycle apparatus at the time of filling the refrigerant immediately increases, and the pressure in the cylinder extremely decreases. For this reason, the carbon dioxide refrigerant cannot be sufficiently sealed in the refrigeration cycle apparatus with a single cylinder connection, and a fully filled cylinder must be connected multiple times to fill the carbon dioxide required for the refrigeration cycle apparatus. Not only does the amount of work increase, but it takes time to fully charge the carbon dioxide refrigerant.

また、二酸化炭素のボンベから冷凍サイクル装置への流入速度を大きくすることを目的として、排出弁やボンベの弁の開度を大きくした場合を考え、図15(a)に点線で示す。図15(a)の点線が示すように、排出弁およびボンベの弁を開いた直後、初期状態aのボンベ内の二酸化炭素冷媒は、各弁の開度が大きいために急激に減圧し、減圧に伴い温度も低下して状態dに至る。一方、冷凍サイクル装置に二酸化炭素冷媒が流入すると、冷凍サイクル装置内の圧力が増加する。すると、ボンベと冷凍サイクル装置との圧力差が小さくなり、それ以上の二酸化炭素冷媒の封入が停滞気味になる。この後、ボンベ内の二酸化炭素冷媒が周囲温度との熱交換により熱を得れば、ボンベ内の冷媒圧力が増加し、ボンベから冷凍サイクル装置へ二酸化炭素冷媒が流入する。二酸化炭素冷媒の流入があれば、再びボンベ内の圧力が低下して温度も低下する。ボンベ内の冷媒状態は、上記の変化を繰り返して状態bに至る。
ボンベ内の二酸化炭素冷媒は、周囲温度と熱交換して徐々に熱量を得ており、減圧による温度低下を緩和するには、温度低下の速度に間に合わない。つまり、弁を開いた直後には二酸化炭素冷媒が冷凍サイクル装置に大量に移動するが、その後は、二酸化炭素冷媒は徐々にしか移動しない。
以上のように、図15において実線や破線で示したように二酸化炭素冷媒を封入した場合でも、点線で示したように排出弁やボンベの弁の開度を大きくした場合でも、二酸化炭素冷媒の封入に時間が掛かることは同じであり、冷凍サイクル装置内に封入できる二酸化炭素の量も同じである。
Further, for the purpose of increasing the inflow rate of carbon dioxide from the cylinder to the refrigeration cycle apparatus, a case where the opening degree of the discharge valve or the cylinder valve is increased is shown by a dotted line in FIG. As shown by the dotted line in FIG. 15 (a), immediately after opening the discharge valve and the cylinder valve, the carbon dioxide refrigerant in the cylinder in the initial state a is suddenly depressurized and depressurized because the opening of each valve is large. As a result, the temperature also decreases to state d. On the other hand, when the carbon dioxide refrigerant flows into the refrigeration cycle apparatus, the pressure in the refrigeration cycle apparatus increases. As a result, the pressure difference between the cylinder and the refrigeration cycle apparatus becomes small, and the entrapment of the carbon dioxide refrigerant becomes stagnant. Thereafter, when the carbon dioxide refrigerant in the cylinder obtains heat by heat exchange with the ambient temperature, the refrigerant pressure in the cylinder increases, and the carbon dioxide refrigerant flows from the cylinder into the refrigeration cycle apparatus. If there is an inflow of carbon dioxide refrigerant, the pressure in the cylinder is lowered again and the temperature is also lowered. The refrigerant state in the cylinder repeats the above change and reaches state b.
The carbon dioxide refrigerant in the cylinder is gradually obtaining heat by exchanging heat with the ambient temperature, and in order to mitigate the temperature decrease due to the reduced pressure, it cannot keep up with the rate of temperature decrease. That is, immediately after opening the valve, a large amount of carbon dioxide refrigerant moves to the refrigeration cycle apparatus, but thereafter, the carbon dioxide refrigerant moves only gradually.
As described above, even when carbon dioxide refrigerant is sealed as shown by the solid line or broken line in FIG. 15 or when the opening degree of the discharge valve or cylinder is increased as shown by the dotted line, the carbon dioxide refrigerant It takes the same time to enclose, and the amount of carbon dioxide that can be enclosed in the refrigeration cycle apparatus is the same.

前述したように、業務用の冷凍サイクル装置の修理や部品交換時には迅速な対応のために、少ないボンベ数で、また短時間で冷凍サイクル装置へ十分な量の二酸化炭素冷媒を充填するために、ボンベに充填する二酸化炭素の量を増やすことを考えると、そのようなボンベの内圧は著しく高くなる。この場合、安全上、操作が困難になることが予想され、ボンベの耐圧も強固にする必要があり経済的に効率的ではない。   As mentioned above, in order to quickly respond to repair and replacement of commercial refrigeration cycle equipment, in order to fill the refrigeration cycle equipment with a sufficient amount of carbon dioxide refrigerant in a short time and in a short time, Considering increasing the amount of carbon dioxide filled in the cylinder, the internal pressure of such a cylinder becomes remarkably high. In this case, it is expected that the operation becomes difficult for safety, and the pressure resistance of the cylinder needs to be strengthened, which is not economically efficient.

本発明は、冷凍サイクル装置が設置されている場所で冷媒を再封入する場合に、上記のような問題を解決するためになされたもので、冷媒を迅速に封入できるような冷凍サイクル装置を得ることを目的とする。   The present invention has been made to solve the above-described problem when re-encapsulating a refrigerant in a place where the refrigeration cycle apparatus is installed, and obtains a refrigeration cycle apparatus capable of quickly enclosing the refrigerant. For the purpose.

本発明に係る冷凍サイクル装置は、流入した冷媒を圧縮して吐出する圧縮機と、圧縮機が吐出した冷媒を凝縮させる凝縮器と、凝縮器からの冷媒を膨張させる膨張弁と、膨張弁からの冷媒を蒸発させて圧縮機に流入させる蒸発器とを備えた循環回路を備えたものであり、さらに蒸発器と圧縮機との間に設けられ、循環回路と外部とを連通させる開閉弁、開閉弁を開く場合に膨張弁の開度を制御する制御回路を備えたことを特徴とする。   A refrigeration cycle apparatus according to the present invention includes a compressor that compresses and discharges an inflowing refrigerant, a condenser that condenses the refrigerant discharged from the compressor, an expansion valve that expands the refrigerant from the condenser, and an expansion valve. An open / close valve that is provided between the evaporator and the compressor and communicates between the circulation circuit and the outside, and an evaporator that causes the refrigerant to evaporate and flow into the compressor. A control circuit for controlling the opening of the expansion valve when the on-off valve is opened is provided.

また、本発明に係る冷凍サイクル装置は、流入した冷媒を圧縮して吐出する圧縮機と、
圧縮機が吐出した冷媒を凝縮させるガスクーラと、ガスクーラからの冷媒を膨張させる膨張弁と、膨張弁からの冷媒を蒸発させて圧縮機に流入させる蒸発器とを備えた循環回路を備えたものであり、さらに圧縮機とガスクーラとの間に設けられて、循環回路と外部とを連通させる開閉弁、開閉弁を開く場合に膨張弁の開度を制御する制御回路を備えたことを特徴とする。
Further, the refrigeration cycle apparatus according to the present invention includes a compressor that compresses and discharges the refrigerant that has flowed in,
A gas cooler that condenses the refrigerant discharged from the compressor, an expansion valve that expands the refrigerant from the gas cooler, and an evaporator that evaporates the refrigerant from the expansion valve and flows into the compressor. And an on-off valve provided between the compressor and the gas cooler for communicating the circulation circuit and the outside, and a control circuit for controlling the opening degree of the expansion valve when the on-off valve is opened. .

本発明によれば、開閉弁を開く場合に制御回路が膨張弁の開度を調整することにより、開閉弁に向かって流れる冷媒により蒸発器が冷却され、その後新たに封入された冷媒は蒸発器で冷却されて圧力の上昇が抑制されるので、冷媒の封入が促進されるという効果を得ることができる。   According to the present invention, when the on-off valve is opened, the control circuit adjusts the opening degree of the expansion valve, whereby the evaporator is cooled by the refrigerant flowing toward the on-off valve, and the newly enclosed refrigerant is Since the increase in pressure is suppressed by the cooling, the effect of facilitating the sealing of the refrigerant can be obtained.

また、本発明によれば、開閉弁を開く場合に制御回路が膨張弁の開度を調整することにより、開閉弁に向かって流れる冷媒によりガスクーラが冷却され、その後新たに封入された冷媒はガスクーラで冷却されて圧力の上昇が抑制されるので、冷媒の封入が促進されるという効果を得ることができる。   Further, according to the present invention, when the opening / closing valve is opened, the control circuit adjusts the opening degree of the expansion valve, whereby the gas cooler is cooled by the refrigerant flowing toward the opening / closing valve, and then the newly sealed refrigerant is removed from the gas cooler. Since the increase in pressure is suppressed by the cooling, the effect of facilitating the sealing of the refrigerant can be obtained.

実施の形態1.
図1は、本発明の実施の形態1に係る冷凍サイクル装置100の構成図である。
図1に示す冷凍サイクル装置100は、圧縮機110、ガスクーラ120、電子式膨張弁130および蒸発器140が配管で接続された循環回路を備え、循環回路の内部を冷媒が循環する。圧縮機110は流入した冷媒を圧縮して吐出し、ガスクーラ120は圧縮機110が吐出した冷媒を凝縮させる凝縮器として動作し、電子式膨張弁130はガスクーラ120からの冷媒を膨張させる膨張弁として動作し、蒸発器140は電子式膨張弁130からの冷媒を蒸発させる。
また、冷凍サイクル装置100は、蒸発器140に送風して蒸発器140内の冷媒の蒸発を促進する送風機150、循環回路の内部と外部とを連通させる開閉弁160、電子式膨張弁130の開度を制御する制御回路170、周囲温度を測定する周囲温度測定器180を備えている。
Embodiment 1 FIG.
FIG. 1 is a configuration diagram of a refrigeration cycle apparatus 100 according to Embodiment 1 of the present invention.
A refrigeration cycle apparatus 100 shown in FIG. 1 includes a circulation circuit in which a compressor 110, a gas cooler 120, an electronic expansion valve 130, and an evaporator 140 are connected by piping, and a refrigerant circulates inside the circulation circuit. The compressor 110 compresses and discharges the refrigerant flowing in, the gas cooler 120 operates as a condenser that condenses the refrigerant discharged from the compressor 110, and the electronic expansion valve 130 functions as an expansion valve that expands the refrigerant from the gas cooler 120. In operation, the evaporator 140 evaporates the refrigerant from the electronic expansion valve 130.
The refrigeration cycle apparatus 100 also opens the blower 150 that blows air to the evaporator 140 and promotes evaporation of the refrigerant in the evaporator 140, the on-off valve 160 that connects the inside and outside of the circulation circuit, and the electronic expansion valve 130. A control circuit 170 for controlling the temperature and an ambient temperature measuring device 180 for measuring the ambient temperature are provided.

冷媒は、冷凍サイクル装置の動作時には、圧縮機110、ガスクーラ120、電子式膨張弁130、蒸発器140、圧縮機110の順に循環回路内を流れており、開閉弁160が開いた時には、開閉弁160を介して外部に流出する。また、開閉弁160を開いて開閉弁160から循環回路内に冷媒を流入させることもできる。   During operation of the refrigeration cycle apparatus, the refrigerant flows through the circulation circuit in the order of the compressor 110, the gas cooler 120, the electronic expansion valve 130, the evaporator 140, and the compressor 110. When the on-off valve 160 is opened, the on-off valve It flows out to the outside through 160. Further, the on-off valve 160 can be opened to allow the refrigerant to flow into the circulation circuit from the on-off valve 160.

制御回路170は、開閉弁160が開いたときに、周囲温度測定器180が測定した周囲温度値を取得して、この周囲温度値に基づき電子式膨張弁130の開度を制御する。図1において、制御回路170と電子式膨張弁130との接続、および制御回路170と周囲温度測定器180との接続を破線で示す。   The control circuit 170 acquires the ambient temperature value measured by the ambient temperature measuring device 180 when the on-off valve 160 is opened, and controls the opening degree of the electronic expansion valve 130 based on the ambient temperature value. In FIG. 1, the connection between the control circuit 170 and the electronic expansion valve 130 and the connection between the control circuit 170 and the ambient temperature measuring device 180 are indicated by broken lines.

図2は、実施の形態1に係る蒸発器140を示す図である。図2(a)は蒸発器140の全体概略図を示し、図2(b)は冷媒管141の断面と同じ方向から見たフィン142を示す。蒸発器140は、内部を冷媒が流れる冷媒管141、アルミあるいは銅などの金属で構成された複数のフィン142を備えている。冷媒管141は、複数の伝熱管141a、流入した冷媒を複数の伝熱管141aに分流させるヘッダー管141b、複数の伝熱管141aから流入した冷媒を合流させて蒸発器140外部に流出させるヘッダー管141cで構成されている。フィン142には複数の伝熱管貫通用穴143が形成され、伝熱管141aは伝熱管貫通用穴143を通っている。伝熱管141aの外周と伝熱管貫通用穴143の円周とはほぼ同じ寸法であり、伝熱管141aは伝熱管間通用穴143の外周に密着するように貫通している。
上記の構成により、蒸発器140に流入した冷媒は、冷媒管141により複数に分岐して流れ、フィン142と熱交換を行った後に合流して蒸発器140の外部に流出する。
FIG. 2 is a diagram showing the evaporator 140 according to the first embodiment. FIG. 2A shows an overall schematic view of the evaporator 140, and FIG. 2B shows the fin 142 viewed from the same direction as the cross section of the refrigerant pipe 141. FIG. The evaporator 140 includes a refrigerant pipe 141 through which a refrigerant flows and a plurality of fins 142 made of a metal such as aluminum or copper. The refrigerant pipe 141 includes a plurality of heat transfer pipes 141a, a header pipe 141b for diverting the inflowing refrigerant to the plurality of heat transfer pipes 141a, and a header pipe 141c for combining the refrigerant flowing in from the plurality of heat transfer pipes 141a to flow out of the evaporator 140. It consists of A plurality of heat transfer tube penetration holes 143 are formed in the fin 142, and the heat transfer tubes 141 a pass through the heat transfer tube penetration holes 143. The outer periphery of the heat transfer tube 141a and the circumference of the heat transfer tube penetration hole 143 have substantially the same dimensions, and the heat transfer tube 141a penetrates so as to be in close contact with the outer periphery of the inter-heat transfer tube passage hole 143.
With the above configuration, the refrigerant that has flowed into the evaporator 140 flows in a branched manner through the refrigerant pipe 141, and after heat exchange with the fins 142, merges and flows out of the evaporator 140.

次に、冷媒排出時の冷凍サイクル装置100の操作内容および冷媒の状態について説明する。
なお、ここでは冷凍サイクル装置に用いる冷媒は二酸化炭素冷媒とし、以降「冷媒」と称する。
図3は、実施の形態1における冷媒排出時の冷媒の状態変化を示す図である。図3において、横軸はエンタルピー、縦軸は絶対圧力を示す。
ここで、圧縮機110からガスクーラ120を経て電子式膨張弁130までの循環回路に滞留する冷媒の状態を状態A、電子式膨張弁130と蒸発器140との間の配管に滞留する冷媒の状態を状態B、蒸発器140と開閉弁160との間の配管に滞留する冷媒の状態を状態C、循環回路の外部に排出された冷媒の状態を状態Dとし、図1および図3に冷媒の状態A,B,C,Dを示す。
Next, the operation content of the refrigeration cycle apparatus 100 when the refrigerant is discharged and the state of the refrigerant will be described.
Here, the refrigerant used in the refrigeration cycle apparatus is a carbon dioxide refrigerant, and is hereinafter referred to as “refrigerant”.
FIG. 3 is a diagram showing a change in state of the refrigerant when the refrigerant is discharged in the first embodiment. In FIG. 3, the horizontal axis represents enthalpy and the vertical axis represents absolute pressure.
Here, the state of the refrigerant staying in the circulation circuit from the compressor 110 through the gas cooler 120 to the electronic expansion valve 130 is the state A, and the state of the refrigerant staying in the pipe between the electronic expansion valve 130 and the evaporator 140 State B, the state of the refrigerant staying in the pipe between the evaporator 140 and the on-off valve 160 is state C, the state of the refrigerant discharged outside the circulation circuit is state D, and FIG. 1 and FIG. States A, B, C, and D are shown.

まず、圧縮機110を停止させた後に開閉弁160を開ける。開閉弁160を開ける際、制御回路170は冷媒排出開始を示す信号を与えられ、この冷媒排出開始信号が入力された制御回路170は電子式膨張弁130を閉じる。また、制御回路170は、周囲温度測定器180が測定した周囲温度値を取得する。
なお、冷媒排出開始信号については、開閉弁160の操作者が外部スイッチを操作して制御回路170に与えても良く、開閉弁160自らが開閉弁160の開閉を検知して、検知結果を冷媒排出開始信号として制御回路170に与えても良い。
First, after the compressor 110 is stopped, the on-off valve 160 is opened. When opening the on-off valve 160, the control circuit 170 is given a signal indicating the start of refrigerant discharge, and the control circuit 170 to which the refrigerant discharge start signal is input closes the electronic expansion valve 130. In addition, the control circuit 170 acquires the ambient temperature value measured by the ambient temperature measuring device 180.
The refrigerant discharge start signal may be given to the control circuit 170 by an operator of the on-off valve 160 by operating an external switch. The on-off valve 160 itself detects the opening / closing of the on-off valve 160, and the detection result is used as the refrigerant. You may give to the control circuit 170 as a discharge start signal.

この後、制御回路170は電子式膨張弁130を開くが、周囲温度値に基づき開度を調整する。圧縮機110から電子式膨張弁130までの循環回路に滞留して状態Aである冷媒は、電子式膨張弁130を通過すると膨張して圧力が低下し、状態Bになる。減圧されて状態Bになった冷媒は、蒸発器140を通過すると蒸発して周囲から熱を得て、状態Cになる。この状態Cの冷媒が開閉弁160から外部に流出すると、大気と同じ圧力である状態Dに遷移する。   Thereafter, the control circuit 170 opens the electronic expansion valve 130, but adjusts the opening degree based on the ambient temperature value. The refrigerant that remains in the circulation circuit from the compressor 110 to the electronic expansion valve 130 and is in the state A expands when passing through the electronic expansion valve 130, and the pressure is reduced to the state B. The refrigerant that has been depressurized to state B evaporates as it passes through the evaporator 140, obtains heat from the surroundings, and enters state C. When the refrigerant in state C flows out from the on-off valve 160, the state transitions to state D, which is the same pressure as the atmosphere.

冷媒は、蒸発器140を通過して状態Bから状態Cに遷移する際に熱交換して周囲から熱を奪うため、蒸発器140は冷媒排出前よりも温度が低下する。電子式膨張弁130による蒸発器140の温度の具体的な制御は、例えば、周囲温度値と電子式膨張弁130の開度との関係を制御回路170に予め設定しておき、制御回路170は、取得した周囲温度値から電子式膨張弁130の開度を調整するというものである。周囲温度値と電子式膨張弁130の開度との関係とは、所定の周囲温度と、蒸発器140出口の飽和液冷媒温度が当該周囲温度値以下になるような電子式膨張弁130の開きとの対応を示す関係である。
なお、蒸発器140が冷媒と熱交換した熱は、主にフィン142や伝熱管141aに蓄積される。また、電子式膨張弁130の開度調整により、飽和液冷媒温度は周囲温度よりも低くなるので、蒸発器140、特にフィン142や伝熱管141aを中心とした温度は、周囲温度よりも低くなる。
When the refrigerant passes through the evaporator 140 and transitions from the state B to the state C, the refrigerant exchanges heat and takes heat away from the surroundings, so the temperature of the evaporator 140 is lower than before the refrigerant is discharged. The specific control of the temperature of the evaporator 140 by the electronic expansion valve 130 is performed by, for example, setting the relationship between the ambient temperature value and the opening of the electronic expansion valve 130 in advance in the control circuit 170. The opening degree of the electronic expansion valve 130 is adjusted from the acquired ambient temperature value. The relationship between the ambient temperature value and the opening of the electronic expansion valve 130 is that the electronic expansion valve 130 is opened so that the predetermined ambient temperature and the saturated refrigerant temperature at the outlet of the evaporator 140 are equal to or lower than the ambient temperature value. It is the relationship which shows correspondence with.
The heat exchanged by the evaporator 140 with the refrigerant is mainly accumulated in the fins 142 and the heat transfer tubes 141a. In addition, since the saturated liquid refrigerant temperature becomes lower than the ambient temperature by adjusting the opening of the electronic expansion valve 130, the temperature around the evaporator 140, particularly the fin 142 and the heat transfer tube 141a, is lower than the ambient temperature. .

次に、冷媒封入時の冷凍サイクル装置100の操作内容および冷媒の状態について説明する。
まず、冷媒封入の前には、循環回路の真空引きが行われる。ところで、一般に、部品交換時のロウ付けにおいては、酸化スケール防止のために冷媒の置換に二酸化炭素が用いられている。この場合には冷媒封入前に装置内の真空引きを十分行う必要がある。しかし、本実施の形態1のように、冷媒自体が二酸化炭素である場合には、冷媒の置換を行う必要がなく、また冷媒を追加して封入することも容易であるため、真空引きを十分行う必要はなく、ボンベ内の冷媒が循環回路内に取り込まれる程度の真空引きを行えば良い。
Next, the operation content of the refrigeration cycle apparatus 100 and the state of the refrigerant when the refrigerant is sealed will be described.
First, before the refrigerant is filled, the circulation circuit is evacuated. By the way, generally, in brazing at the time of parts replacement, carbon dioxide is used for refrigerant replacement to prevent oxidation scale. In this case, it is necessary to sufficiently evacuate the apparatus before filling the refrigerant. However, when the refrigerant itself is carbon dioxide as in the first embodiment, it is not necessary to replace the refrigerant, and it is easy to add and enclose the refrigerant. It is not necessary to perform this, and it is sufficient to perform vacuuming so that the refrigerant in the cylinder is taken into the circulation circuit.

冷媒封入の際、冷媒の入ったボンベを開閉弁160に接続して、開閉弁160およびボンベを開けば、冷媒がボンベから循環回路内に流入する。
図4は、冷媒封入時における冷媒の状態変化を示す図である。図4(a)は、ボンベ内および冷凍サイクル装置の循環回路内の二酸化炭素冷媒の状態変化を示す図であり、図4(b)は図4(a)の大気圧付近を拡大して示した図である。図4(a)、(b)のいずれにおいても、横軸はエンタルピー、縦軸は絶対圧力を示す。また、図4において、実線はボンベ内の冷媒の状態の変化を示し、冷媒封入前を状態E、冷媒封入時の最終状態を状態Fとする。破線は循環回路内の冷媒の状態の変化を示し、冷媒封入前を状態G、冷媒封入時の途中の状態を状態H、最終状態を状態Iとする。ここでは周囲温度が40℃程度であり、ボンベ内の冷媒温度も同程度である場合を想定する。
When the refrigerant is filled, if the cylinder containing the refrigerant is connected to the on-off valve 160 and the on-off valve 160 and the cylinder are opened, the refrigerant flows from the cylinder into the circulation circuit.
FIG. 4 is a diagram illustrating a change in state of the refrigerant when the refrigerant is sealed. FIG. 4 (a) is a diagram showing changes in the state of carbon dioxide refrigerant in the cylinder and in the circulation circuit of the refrigeration cycle apparatus, and FIG. 4 (b) is an enlarged view of the vicinity of atmospheric pressure in FIG. 4 (a). It is a figure. 4A and 4B, the horizontal axis indicates enthalpy and the vertical axis indicates absolute pressure. In FIG. 4, the solid line indicates the change in the state of the refrigerant in the cylinder, and state E is the state before the refrigerant is filled and state F is the final state when the refrigerant is filled. A broken line indicates a change in the state of the refrigerant in the circulation circuit, and state G before the refrigerant filling, state H during the refrigerant filling, and state I as the final state. Here, it is assumed that the ambient temperature is about 40 ° C. and the refrigerant temperature in the cylinder is about the same.

冷媒がボンベから循環回路に流入すると、状態Eであったボンベ内の冷媒は、温度を一定に維持、つまり周囲温度と略同じ温度のまま、状態Fに至る。このとき、冷媒の密度および圧力は、状態Fに近づくにつれて低下していく。   When the refrigerant flows into the circulation circuit from the cylinder, the refrigerant in the cylinder in the state E maintains the temperature constant, that is, reaches the state F with the temperature substantially the same as the ambient temperature. At this time, the density and pressure of the refrigerant decrease as the state F is approached.

一方、状態Gであった循環回路内の冷媒は、ボンベからの冷媒の流入により圧力を増す。冷媒は、ボンベから開閉弁160に流入されたときには超臨界状態であるが、周囲温度よりも温度の低い蒸発器140で冷却されて気液二相状態や液相状態になる。冷媒が超臨界状態であるときよりも気液二相状態等であるときの方が冷媒の圧力が低いので、冷媒封入による循環回路内の圧力の上昇が抑制される。図4の破線が示すように、封入された冷媒は、伝熱管121aやフィン142等と同等の温度を維持する、また、封入とともに循環回路内の冷媒圧力は上昇するが、やがて圧力上昇が停止し(状態H)、液相へと変化し、最終的には状態Iに至る。
このように、循環回路内の冷媒の圧力上昇が抑制され、ボンベ内と循環回路内との圧力差が維持されるので、ボンベ内の冷媒は圧力の低い循環回路に流入しやすくなる。
On the other hand, the refrigerant in the circulation circuit in the state G increases in pressure due to the inflow of refrigerant from the cylinder. The refrigerant is in a supercritical state when it flows from the cylinder into the on-off valve 160, but is cooled by the evaporator 140 having a temperature lower than the ambient temperature to be in a gas-liquid two-phase state or a liquid phase state. Since the pressure of the refrigerant is lower when the refrigerant is in the gas-liquid two-phase state or the like than when it is in the supercritical state, an increase in the pressure in the circulation circuit due to the refrigerant filling is suppressed. As shown by the broken line in FIG. 4, the enclosed refrigerant maintains the same temperature as the heat transfer tubes 121a, the fins 142, and the like, and the refrigerant pressure in the circulation circuit rises with the enclosure, but the pressure increase eventually stops. (State H), the liquid phase is changed, and finally state I is reached.
Thus, the pressure increase of the refrigerant in the circulation circuit is suppressed and the pressure difference between the cylinder and the circulation circuit is maintained, so that the refrigerant in the cylinder easily flows into the circulation circuit having a low pressure.

次に、本実施の形態1において、ボンベを1本使った場合に封入できる冷媒の量を計算する。
ここでは、「背景技術」欄で従来の冷媒封入方法を説明した場合と同様、冷凍サイクル装置100の内容積が約30L、ボンベについては、内容積が約9L、初期の状態の充填量が7.0Kgとする。これにより、ボンベ内は、周囲温度40℃で圧力14.7MPaになる。また、冷媒封入前の蒸発器140の温度は約10℃とする。
このとき、循環回路およびボンベ内の最終的な圧力は4.5MPaとなり、循環回路内へ移動した冷媒は6.12kgとなる。蒸発器140が周囲温度よりも低い場合の二酸化炭素の封入量は、従来の冷媒封入方法よりも増えている。
Next, in this Embodiment 1, the quantity of the refrigerant | coolant which can be enclosed when one cylinder is used is calculated.
Here, as in the case of explaining the conventional refrigerant filling method in the “Background Art” column, the internal volume of the refrigeration cycle apparatus 100 is about 30 L, and the cylinder has an internal volume of about 9 L, and the initial filling amount is 7 L. 0.0 kg. As a result, the pressure inside the cylinder is 14.7 MPa at an ambient temperature of 40 ° C. Moreover, the temperature of the evaporator 140 before refrigerant | coolant enclosure shall be about 10 degreeC.
At this time, the final pressure in the circulation circuit and the cylinder is 4.5 MPa, and the refrigerant that has moved into the circulation circuit is 6.12 kg. The amount of carbon dioxide enclosed when the evaporator 140 is lower than the ambient temperature is larger than that of the conventional refrigerant filling method.

以上のように、本実施の形態1においては、冷媒排出時に制御回路170が周囲温度値に基づき電子式膨張弁130の開度を調整し、蒸発器140の温度を低下させるので、冷凍サイクル装置100内に流入した冷媒が蒸発器140で冷却されて気液二相状態または液相状態に変化し、循環回路内の圧力の上昇が抑制される。これにより、ボンベから循環回路への冷媒封入を促進することができる。   As described above, in the first embodiment, the control circuit 170 adjusts the opening degree of the electronic expansion valve 130 based on the ambient temperature value and lowers the temperature of the evaporator 140 when the refrigerant is discharged. The refrigerant that has flowed into 100 is cooled by the evaporator 140 and changes to a gas-liquid two-phase state or a liquid-phase state, thereby suppressing an increase in pressure in the circulation circuit. Thereby, the refrigerant | coolant enclosure from a cylinder to a circulation circuit can be accelerated | stimulated.

ところで、上記実施の形態1では、制御回路170は、蒸発器140出口の飽和液冷媒温度が当該周囲温度値以下になるように電子式膨張弁130の開度を調整していた。しかし、冷媒は、冷凍サイクル装置に封入された際に臨界温度を超えずに超臨界状態にならなければ、封入が促進されるので、本実施の形態1において制御回路170が蒸発器140出口の飽和液冷媒温度が冷媒の臨界温度以下になるように電子式膨張弁130の開度を調整するように構成しても良い。また、制御回路170は、周囲温度または冷媒の臨界温度ではなく、所定の温度以下を参照し、飽和液冷媒温度が所定の温度以下になるように電子式膨張弁130の開度を調整しても良い。   In the first embodiment, the control circuit 170 adjusts the opening degree of the electronic expansion valve 130 so that the saturated liquid refrigerant temperature at the outlet of the evaporator 140 is equal to or lower than the ambient temperature value. However, if the refrigerant does not reach the supercritical state without exceeding the critical temperature when sealed in the refrigeration cycle apparatus, the sealing is promoted, so in the first embodiment, the control circuit 170 is connected to the outlet of the evaporator 140. You may comprise so that the opening degree of the electronic expansion valve 130 may be adjusted so that saturated liquid refrigerant temperature may become below the critical temperature of a refrigerant | coolant. In addition, the control circuit 170 refers to not the ambient temperature or the critical temperature of the refrigerant but a predetermined temperature or lower, and adjusts the opening of the electronic expansion valve 130 so that the saturated liquid refrigerant temperature is lower than the predetermined temperature. Also good.

また、上記実施の形態1では、圧縮機110の流路抵抗が大きく、冷媒は圧縮機110の吸入側から開閉弁160に向かって流れることがないという前提で、冷媒排出時の循環回路内の冷媒の流れが、圧縮機110、凝縮器120、電子式膨張弁130、蒸発器140、開閉弁160の順であることと説明していた。しかし、圧縮機110の流路抵抗が小さい場合や、冷媒を圧縮機110からガスヒーター120に向かって確実に流した場合には、圧縮機110の前後、例えば圧縮機110と開閉弁160との間や圧縮機110とガスヒータ120との間などに逆止弁を設けても良い。逆止弁は、圧縮機110の吸入側から開閉弁160への冷媒の流れを防ぐものである。   In the first embodiment, the flow path resistance of the compressor 110 is large, and the refrigerant does not flow from the suction side of the compressor 110 toward the on-off valve 160. It has been described that the flow of the refrigerant is in the order of the compressor 110, the condenser 120, the electronic expansion valve 130, the evaporator 140, and the on-off valve 160. However, when the flow path resistance of the compressor 110 is small, or when the refrigerant is surely flowed from the compressor 110 toward the gas heater 120, before and after the compressor 110, for example, between the compressor 110 and the on-off valve 160, A check valve may be provided between the compressor 110 and the gas heater 120. The check valve prevents the refrigerant from flowing from the suction side of the compressor 110 to the on-off valve 160.

また、上記実施の形態1では、冷媒排出時には圧縮機110を停止させた後に電子式膨張弁130を閉じ、開閉弁160を開ける操作をしていた。しかし、電子式膨張弁130で調整する状態Aの冷媒を循環回路内に多く保持しておくために、圧縮機110を停止する前に電子式膨張弁130を閉じるようにしても良い。この場合、循環する冷媒の流れが電子式膨張弁130で止められるので、冷媒はガスクーラ120等に保持される。つまり、冷媒排出時に電子式膨張弁130および蒸発器140を通過する冷媒の量が増え、蒸発器140の冷却量が増えるので、冷媒封入時の冷媒冷却を強化して、冷媒封入もさらに促進することができる。   In the first embodiment, when the refrigerant is discharged, the compressor 110 is stopped and then the electronic expansion valve 130 is closed and the on-off valve 160 is opened. However, the electronic expansion valve 130 may be closed before the compressor 110 is stopped in order to keep a large amount of the refrigerant in the state A adjusted by the electronic expansion valve 130 in the circulation circuit. In this case, since the flow of the circulating refrigerant is stopped by the electronic expansion valve 130, the refrigerant is held in the gas cooler 120 or the like. That is, when the refrigerant is discharged, the amount of refrigerant passing through the electronic expansion valve 130 and the evaporator 140 is increased, and the amount of cooling of the evaporator 140 is increased. Therefore, the cooling of the refrigerant at the time of charging the refrigerant is enhanced and the cooling of the refrigerant is further promoted. be able to.

なお、従来の冷凍サイクル装置のように電子式膨張弁130で圧力制御を行わずに二酸化炭素冷媒を排出すると、二酸化炭素冷媒が開閉弁160の付近で急激に減圧する。開閉弁160の付近や冷凍サイクル装置の設置面などに二酸化炭素が到達すると、その付近にドライアイスが生成されて付着する場合がある。このように付着したドライアイスが気化すると、付着面を粉砕することもある。しかし、上記実施の形態1では、制御装置170が電子式膨張弁130の開度を制御するので、冷媒排出時の二酸化炭素は循環回路内で減圧して蒸発し、ドライアイスが生成されることもなく、ドライアイスが付着した面が粉砕されることもない。   Note that when the carbon dioxide refrigerant is discharged without pressure control by the electronic expansion valve 130 as in the conventional refrigeration cycle apparatus, the carbon dioxide refrigerant rapidly depressurizes in the vicinity of the on-off valve 160. When carbon dioxide reaches the vicinity of the on-off valve 160 or the installation surface of the refrigeration cycle apparatus, dry ice may be generated and adhered to the vicinity. When the attached dry ice is vaporized, the attached surface may be crushed. However, in the first embodiment, since the control device 170 controls the opening degree of the electronic expansion valve 130, the carbon dioxide when the refrigerant is discharged is depressurized and evaporated in the circulation circuit, and dry ice is generated. In addition, the surface with dry ice is not crushed.

さらに、上記実施の形態1では、冷媒が二酸化炭素である場合について説明したが、冷媒がHFC系冷媒の場合にも適用できる。つまり、周囲温度やHFC冷媒の臨界温度を考慮して制御回路170を動作させ、冷媒排出時の電子式膨張弁130の開度を調整して蒸発器140を冷却すれば、封入時のボンベと循環回路内との間の圧力差が確保されるので、冷媒が二酸化炭素である場合と同様、冷媒の封入を促進できるという効果を得られる。   Furthermore, although the case where the refrigerant is carbon dioxide has been described in the first embodiment, the present invention can also be applied to the case where the refrigerant is an HFC refrigerant. In other words, if the control circuit 170 is operated in consideration of the ambient temperature and the critical temperature of the HFC refrigerant, and the evaporator 140 is cooled by adjusting the opening of the electronic expansion valve 130 when the refrigerant is discharged, Since the pressure difference with the inside of the circulation circuit is ensured, the effect of facilitating the sealing of the refrigerant can be obtained as in the case where the refrigerant is carbon dioxide.

実施の形態2.
実施の形態1では、制御回路170は周囲温度に基づき電子式開閉弁130の開度を調整していた。しかし、制御回路170について、周囲温度だけでなく、冷媒圧力も参照して電子式開閉弁130の開度を調整するよう構成しても良い。
図5は、本発明の実施の形態2に係る冷凍サイクル装置100の構成図である。図5に示す実施の形態2に係る冷凍サイクル装置100は、実施の形態1に係る冷凍サイクル装置100に冷媒圧力測定器200を設けたものである。図1に示す実施の形態1に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 2. FIG.
In the first embodiment, the control circuit 170 adjusts the opening degree of the electronic on-off valve 130 based on the ambient temperature. However, the control circuit 170 may be configured to adjust the opening degree of the electronic on-off valve 130 with reference to not only the ambient temperature but also the refrigerant pressure.
FIG. 5 is a configuration diagram of the refrigeration cycle apparatus 100 according to Embodiment 2 of the present invention. The refrigeration cycle apparatus 100 according to Embodiment 2 shown in FIG. 5 is obtained by providing a refrigerant pressure measuring device 200 to the refrigeration cycle apparatus 100 according to Embodiment 1. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 1 shown in FIG. 1, and the description is abbreviate | omitted.

冷媒圧力測定器200は、蒸発器140と開閉弁160との間に設けられ、冷媒の圧力を測定するものである。すなわち、冷媒圧力測定器200は、蒸発器140から排出された冷媒の圧力を測定しており、測定した冷媒圧力値を制御装置170に送信する。   The refrigerant pressure measuring device 200 is provided between the evaporator 140 and the on-off valve 160 and measures the pressure of the refrigerant. That is, the refrigerant pressure measuring device 200 measures the pressure of the refrigerant discharged from the evaporator 140 and transmits the measured refrigerant pressure value to the control device 170.

次に、冷媒排出時の冷凍サイクル装置100の操作内容および冷媒の状態について説明する。なお、実施の形態1と同一の内容については説明を省略する。
実施の形態1にて説明した図3の通り、冷媒排出時に膨張した状態Bの冷媒は、蒸発器140で空気と熱交換して蒸発し、状態Cに至る。ここで状態Aから状態Bになった冷媒は、電子式膨張弁130を通過したものであり、電子式膨張弁130の開度は、制御回路170により調整される。
Next, the operation content of the refrigeration cycle apparatus 100 when the refrigerant is discharged and the state of the refrigerant will be described. In addition, description is abbreviate | omitted about the content same as Embodiment 1. FIG.
As illustrated in FIG. 3 described in the first embodiment, the refrigerant in the state B that is expanded when the refrigerant is discharged is exchanged with the air by the evaporator 140 to evaporate and reach the state C. Here, the refrigerant that has changed from state A to state B has passed through the electronic expansion valve 130, and the opening degree of the electronic expansion valve 130 is adjusted by the control circuit 170.

なお、制御回路170の電子式膨張弁130の調整は、状態Cの冷媒の圧力から導かれる飽和液冷媒温度が、周囲温度よりも低くなることを目的として行うものである。つまり、制御回路170は、周囲温度測定器180が測定した周囲温度の値を周囲温度測定器180から取得するとともに、冷媒圧力測定器200が測定した状態Cの冷媒の圧力値を冷媒圧力測定器200から取得し、冷媒圧力値から飽和液冷媒温度を導いて、この飽和液冷媒温度が周囲温度値よりも小さくなるように電子式膨張弁130の開度を調整する。   The adjustment of the electronic expansion valve 130 of the control circuit 170 is performed for the purpose of lowering the saturated liquid refrigerant temperature derived from the pressure of the refrigerant in the state C to be lower than the ambient temperature. In other words, the control circuit 170 obtains the ambient temperature value measured by the ambient temperature measuring device 180 from the ambient temperature measuring device 180, and the refrigerant pressure measuring device 200 obtains the pressure value of the refrigerant in the state C measured by the refrigerant pressure measuring device 200. 200, the saturated liquid refrigerant temperature is derived from the refrigerant pressure value, and the opening degree of the electronic expansion valve 130 is adjusted so that the saturated liquid refrigerant temperature becomes smaller than the ambient temperature value.

ここで、電子式膨張弁130の開度の調整により冷媒の状態変化を調整する例を説明する。
なお、電子式膨張弁130の開度を変更すると、電子式膨張弁130から蒸発器140に至って、さらに開閉弁160まで流れる冷媒の速度や量も変化するため、冷媒の状態変化の要因は電子式膨張弁130の開度だけではないと言える。しかし、ここでは、冷媒の速度や量の変化量については一定であると仮定する。
Here, the example which adjusts the state change of a refrigerant | coolant by adjustment of the opening degree of the electronic expansion valve 130 is demonstrated.
If the opening degree of the electronic expansion valve 130 is changed, the speed and amount of the refrigerant flowing from the electronic expansion valve 130 to the evaporator 140 and further to the on-off valve 160 also change. It can be said that it is not only the opening degree of the type expansion valve 130. However, here, it is assumed that the amount of change in the speed and amount of the refrigerant is constant.

まず、冷媒圧力値から導いた飽和液冷媒温度が周囲温度値よりも高い場合には、蒸発器140の温度も周囲温度よりも高い。そのため、制御回路170は、電子式膨張弁130の開度を現在よりも小さくする。これにより、状態Bの冷媒圧力はさらに低下するので、冷媒が蒸発器140で熱交換すると、電子式膨張弁130の開度変更前よりも蒸発器140の温度が低下する。
また、冷媒圧力値から導いた飽和液冷媒温度が周囲温度値よりも低い場合には、蒸発器140の温度も周囲温度よりも低い。このとき、電子式膨張弁130の開度は、蒸発器140を冷却するには十分でも、冷媒を排出するには小さすぎる可能性がある。電子式膨張弁130の開度が小さいと冷媒排出に時間が掛かるため、制御回路170は、電子式膨張弁130の開度を現在よりも大きくする。つまり、制御回路170は、冷媒圧力値から導いた飽和液冷媒温度が周囲温度値よりも低いままで、電子式膨張弁130の開度を大きくする。これにより、電子式膨張弁130による膨張率は低下して、状態Bの冷媒圧力は上昇するが、蒸発器140の出口付近での飽和液冷媒温度は周囲温度値よりも低いので、蒸発器140を十分冷却することができる。
First, when the saturated liquid refrigerant temperature derived from the refrigerant pressure value is higher than the ambient temperature value, the temperature of the evaporator 140 is also higher than the ambient temperature. Therefore, the control circuit 170 makes the opening degree of the electronic expansion valve 130 smaller than the present time. As a result, the refrigerant pressure in the state B further decreases, so that when the refrigerant exchanges heat with the evaporator 140, the temperature of the evaporator 140 is lower than before the opening of the electronic expansion valve 130 is changed.
When the saturated liquid refrigerant temperature derived from the refrigerant pressure value is lower than the ambient temperature value, the temperature of the evaporator 140 is also lower than the ambient temperature. At this time, the opening degree of the electronic expansion valve 130 may be sufficient to cool the evaporator 140 but may be too small to discharge the refrigerant. When the opening degree of the electronic expansion valve 130 is small, it takes time to discharge the refrigerant. Therefore, the control circuit 170 makes the opening degree of the electronic expansion valve 130 larger than the current opening degree. That is, the control circuit 170 increases the opening degree of the electronic expansion valve 130 while the saturated liquid refrigerant temperature derived from the refrigerant pressure value remains lower than the ambient temperature value. As a result, the expansion rate by the electronic expansion valve 130 decreases and the refrigerant pressure in the state B increases, but the saturated liquid refrigerant temperature near the outlet of the evaporator 140 is lower than the ambient temperature value. Can be cooled sufficiently.

冷媒封入時の操作および動作は実施の形態1と同じであり、開閉弁160から循環回路に流入した冷媒は、蒸発器140により冷却されるので、ボンベ内の冷媒は圧力の低い循環回路に流入しやすくなる。   The operation and operation at the time of filling the refrigerant is the same as in the first embodiment, and the refrigerant flowing into the circulation circuit from the on-off valve 160 is cooled by the evaporator 140, so that the refrigerant in the cylinder flows into the circulation circuit having a low pressure. It becomes easy to do.

以上のように、本実施の形態2によれば、制御装置170が、冷媒圧力から導いた飽和液冷媒温度、および周囲温度値に基づき電子式膨張弁130の開度を調整するので、冷媒排出時に蒸発器140を冷却することで冷媒の封入を効率的に促進できるという効果を得られるだけでなく、冷凍サイクル装置100の冷媒排出の時間を適切に調整できるという効果を得ることができる。   As described above, according to the second embodiment, the controller 170 adjusts the opening degree of the electronic expansion valve 130 based on the saturated liquid refrigerant temperature derived from the refrigerant pressure and the ambient temperature value. Sometimes, cooling the evaporator 140 not only provides an effect of efficiently accelerating the charging of the refrigerant, but also provides an effect of appropriately adjusting the refrigerant discharge time of the refrigeration cycle apparatus 100.

実施の形態3.
実施の形態2では、制御回路170は冷媒圧力値から導いた飽和液冷媒温度と周囲温度値とを比較して電子膨張弁130の開度を調整していたが、実施の形態3では、電子膨張弁130の開度の調整に、冷媒温度値と周囲温度値とを用いる。
図6は、本発明の実施の形態3に係る冷凍サイクル装置100の構成図である。図6に示す実施の形態3に係る冷凍サイクル装置100は、実施の形態1に係る冷凍サイクル装置100に冷媒温度測定器300を設けたものである。図1に示す実施の形態1に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 3 FIG.
In the second embodiment, the control circuit 170 compares the saturated liquid refrigerant temperature derived from the refrigerant pressure value with the ambient temperature value and adjusts the opening degree of the electronic expansion valve 130. The refrigerant temperature value and the ambient temperature value are used to adjust the opening degree of the expansion valve 130.
FIG. 6 is a configuration diagram of the refrigeration cycle apparatus 100 according to Embodiment 3 of the present invention. A refrigeration cycle apparatus 100 according to Embodiment 3 shown in FIG. 6 is obtained by providing a refrigerant temperature measuring device 300 to the refrigeration cycle apparatus 100 according to Embodiment 1. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 1 shown in FIG. 1, and the description is abbreviate | omitted.

冷媒温度測定器300は、蒸発器140と開閉弁160との間に設けられ、冷媒の温度を測定するものである。すなわち、冷媒温度測定器300は、蒸発器140から排出された冷媒の温度を測定しており、測定した冷媒温度値を制御回路170に送信する。   The refrigerant temperature measuring device 300 is provided between the evaporator 140 and the on-off valve 160, and measures the temperature of the refrigerant. That is, the refrigerant temperature measuring device 300 measures the temperature of the refrigerant discharged from the evaporator 140 and transmits the measured refrigerant temperature value to the control circuit 170.

実施の形態3に係る制御回路170は、状態Cの冷媒の温度が周囲温度値よりも低くなるように電子式膨張弁130の開度を制御する。
なお、ここでは、制御回路170は冷媒温度値が周囲温度値よりも低くなるように電子式膨張弁130の開度を調整する。しかし、冷却された蒸発器140は周囲の雰囲気により温度が上昇する可能性があることや、蒸発器140を効率良く冷やすこと考え、冷媒温度値が周囲温度値よりも所定の温度、例えば5度低くなるように制御しても良い。
The control circuit 170 according to the third embodiment controls the opening degree of the electronic expansion valve 130 so that the temperature of the refrigerant in the state C is lower than the ambient temperature value.
Here, the control circuit 170 adjusts the opening of the electronic expansion valve 130 so that the refrigerant temperature value is lower than the ambient temperature value. However, the temperature of the cooled evaporator 140 may rise due to the ambient atmosphere, and the refrigerant temperature value is set to a predetermined temperature, for example, 5 degrees from the ambient temperature value in consideration of cooling the evaporator 140 efficiently. You may control so that it may become low.

また、ここでは、冷媒温度測定器300を蒸発器140と開閉弁160との間に設けたが、冷媒温度測定器300を、蒸発器140の出口側の冷媒配管や、開閉弁160の上流で開閉弁160の近傍に設けても良い。また、冷媒温度測定器300の設置箇所により循環回路内の冷媒温度が異なることを考慮して、電子式膨張弁130を、冷媒温度、周囲温度値および冷媒温度測定器300の設置箇所に基づき電子式膨張弁130の開度を調整するような構成にしても良い。   Further, here, the refrigerant temperature measuring device 300 is provided between the evaporator 140 and the on-off valve 160, but the refrigerant temperature measuring device 300 is installed upstream of the on-off valve 160 and the refrigerant piping on the outlet side of the evaporator 140. You may provide in the vicinity of the on-off valve 160. Further, considering that the refrigerant temperature in the circulation circuit varies depending on the installation location of the refrigerant temperature measuring device 300, the electronic expansion valve 130 is electronically operated based on the refrigerant temperature, the ambient temperature value, and the installation location of the refrigerant temperature measuring device 300. The opening of the type expansion valve 130 may be adjusted.

以上のように、本実施の形態3によれば、蒸発器140の出口における状態Cの冷媒温度値と周囲温度値とに基づき電子式膨張弁130を調整した場合にも、実施の形態2において冷媒圧力値と周囲温度値とに基づき制御した場合と同様、冷媒排出時に蒸発器140を冷却することができる。これにより、冷媒の封入を効率的に促進できるという効果を得られるだけでなく、冷凍サイクル装置100の冷媒排出の時間を適切に調整できるという効果を得ることができる。   As described above, according to the third embodiment, even when the electronic expansion valve 130 is adjusted based on the refrigerant temperature value in the state C at the outlet of the evaporator 140 and the ambient temperature value, As in the case of control based on the refrigerant pressure value and the ambient temperature value, the evaporator 140 can be cooled when the refrigerant is discharged. Thereby, not only the effect that the enclosure of the refrigerant can be efficiently promoted but also the effect that the refrigerant discharge time of the refrigeration cycle apparatus 100 can be appropriately adjusted can be obtained.

ところで、上記実施の形態3では、制御回路170は、周囲温度値と冷媒温度値とを比較して電子式膨張弁130の開度を調整していたが、以降では、冷凍サイクル装置100に係るもう一つの形態を示す。
図7は、本発明の実施の形態3におけるもう一つの形態である冷凍サイクル装置100の蒸発器140を示す図である。実施の形態3に係るもう一つの形態は、図6に示すような冷媒温度測定器300の替わりに、蒸発器140に温度測定器301を設けたものである。なお、図1や図2に示す実施の形態1に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
By the way, in Embodiment 3 described above, the control circuit 170 compares the ambient temperature value and the refrigerant temperature value to adjust the opening of the electronic expansion valve 130. Hereinafter, the control circuit 170 relates to the refrigeration cycle apparatus 100. Another form is shown.
FIG. 7 is a diagram showing an evaporator 140 of the refrigeration cycle apparatus 100, which is another embodiment according to Embodiment 3 of the present invention. In another embodiment according to the third embodiment, a temperature measuring device 301 is provided in the evaporator 140 instead of the refrigerant temperature measuring device 300 as shown in FIG. In addition, the same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 1 shown in FIG.1 and FIG.2, and the description is abbreviate | omitted.

図7において、温度測定器301は、複数のフィン142のうちの2枚の間に挟みこまれるように設置され、取り付けられているフィン142の温度を測定するものである。
一般に、冷媒排出時、冷媒は蒸発器140で熱交換して熱を取得するので、冷媒排出が進むにつれて、フィン142の温度は低下する。
そこで、制御回路170は、温度測定器301が測定したフィン142の温度が、周囲温度測定器180が測定した周囲温度値よりも小さくなるように電子式膨張弁130の開度を制御する。
In FIG. 7, the temperature measuring device 301 is installed so as to be sandwiched between two of the plurality of fins 142 and measures the temperature of the attached fins 142.
Generally, when the refrigerant is discharged, the refrigerant exchanges heat with the evaporator 140 to acquire heat, so that the temperature of the fin 142 decreases as the refrigerant discharge proceeds.
Therefore, the control circuit 170 controls the opening degree of the electronic expansion valve 130 so that the temperature of the fin 142 measured by the temperature measuring device 301 is smaller than the ambient temperature value measured by the ambient temperature measuring device 180.

ただし、蒸発器140の冷却により、使用する冷媒が蒸発器140の冷媒管141の中で凍結させないことが重要である。そのためには、制御回路170を、フィン142の温度が二酸化炭素の凝固点−56.6℃以上になるよう、また圧力0.518MPaになるよう制御するよう構成する。   However, it is important that the refrigerant to be used is not frozen in the refrigerant pipe 141 of the evaporator 140 by cooling the evaporator 140. For that purpose, the control circuit 170 is configured to control the temperature of the fin 142 so that the freezing point of carbon dioxide is −56.6 ° C. or more and the pressure is 0.518 MPa.

このように、冷媒温度値の替わりにフィンの温度を測定した場合でも、蒸発器140の冷却の度合いが把握できるため、冷媒温度値と周囲温度値とに基づき電子式膨張弁130を制御した場合と同様の効果を得ることができる。   Thus, even when the temperature of the fin is measured instead of the refrigerant temperature value, the degree of cooling of the evaporator 140 can be grasped, and thus the electronic expansion valve 130 is controlled based on the refrigerant temperature value and the ambient temperature value. The same effect can be obtained.

実施の形態4.
図8は、本発明の実施の形態4に係る冷凍サイクル装置100の構成図である。図8に示す冷凍サイクル装置100は、実施の形態1に係る冷凍サイクル装置100に、実施の形態2に係る冷媒圧力測定器200、および実施の形態3に係る冷媒温度測定器300を備えたものである。図1、図5および図6に示す実施の形態1、2および3に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 4 FIG.
FIG. 8 is a configuration diagram of the refrigeration cycle apparatus 100 according to Embodiment 4 of the present invention. The refrigeration cycle apparatus 100 shown in FIG. 8 includes the refrigeration cycle apparatus 100 according to the first embodiment, the refrigerant pressure measuring instrument 200 according to the second embodiment, and the refrigerant temperature measuring instrument 300 according to the third embodiment. It is. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 1, 2, and 3 shown in FIG.1, FIG5 and FIG.6, and the description is abbreviate | omitted.

制御回路170は、状態Cの冷媒について、冷媒圧力測定器200から冷媒圧力値を取得して、この冷媒圧力値から冷媒の飽和液冷媒温度を導き、さらに冷媒温度測定器300から冷媒温度値を取得する。また、周囲温度測定器180から周囲温度値を取得し、冷媒圧力値、冷媒温度値および周囲温度値に基づき、状態Cの冷媒の飽和液冷媒温度が周囲温度値よりも低くなるように電子式膨張弁130の開度を調整する。   The control circuit 170 acquires the refrigerant pressure value from the refrigerant pressure measuring device 200 for the refrigerant in the state C, derives the saturated liquid refrigerant temperature of the refrigerant from the refrigerant pressure value, and further calculates the refrigerant temperature value from the refrigerant temperature measuring device 300. get. In addition, the ambient temperature value is obtained from the ambient temperature measuring device 180, and based on the refrigerant pressure value, the refrigerant temperature value, and the ambient temperature value, the saturated liquid refrigerant temperature of the refrigerant in the state C is set to be lower than the ambient temperature value. The opening degree of the expansion valve 130 is adjusted.

以上のように、実施の形態4によれば、状態Cの飽和液冷媒温度と周囲温度値とを比較して電子式膨張弁130の開度を調整する場合に、冷媒圧力値および冷媒温度値とを参照するので、電子式膨張弁130の開度の調整を排出時間や蒸発器140の冷却レベルなどの観点から効率良く行うことができる。   As described above, according to the fourth embodiment, when the opening degree of the electronic expansion valve 130 is adjusted by comparing the saturated liquid refrigerant temperature in the state C and the ambient temperature value, the refrigerant pressure value and the refrigerant temperature value. Therefore, the opening degree of the electronic expansion valve 130 can be adjusted efficiently from the viewpoint of the discharge time, the cooling level of the evaporator 140, and the like.

ところで、上記実施の形態4では、冷媒温度測定器300を用いて状態Cの冷媒温度値を取得したが、冷媒温度測定器300の替わりに、温度測定器301をフィン142に設けても良い。つまり、制御装置170は、状態Cの冷媒圧力値、フィン142の温度、および周囲温度値に基づき電子式膨張弁130の開度を調整することになる。この場合においても、状態Cの冷媒温度値を用いて電子式膨張弁130の開度を調整した場合と同様に、細密な調整をすることができる。   By the way, in the said Embodiment 4, the refrigerant | coolant temperature value of the state C was acquired using the refrigerant | coolant temperature measuring device 300, However, You may provide the temperature measuring device 301 in the fin 142 instead of the refrigerant | coolant temperature measuring device 300. FIG. That is, the control device 170 adjusts the opening degree of the electronic expansion valve 130 based on the refrigerant pressure value in the state C, the temperature of the fin 142, and the ambient temperature value. In this case as well, fine adjustment can be performed as in the case where the opening degree of the electronic expansion valve 130 is adjusted using the refrigerant temperature value in the state C.

実施の形態5
図9は、本発明の実施の形態5に係る冷凍サイクル装置100の構成図である。図9に示す実施の形態5に係る冷凍サイクル装置100は、実施の形態4に係る冷凍サイクル装置100に開閉弁160の開度を調整する開度調整部161を備えたものである。図8に示す実施の形態4に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 5
FIG. 9 is a configuration diagram of a refrigeration cycle apparatus 100 according to Embodiment 5 of the present invention. The refrigeration cycle apparatus 100 according to Embodiment 5 shown in FIG. 9 includes the refrigeration cycle apparatus 100 according to Embodiment 4 and an opening degree adjustment unit 161 that adjusts the opening degree of the on-off valve 160. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 4 shown in FIG. 8, and the description is abbreviate | omitted.

制御回路170は、状態Cの冷媒圧力値および冷媒温度値と周囲温度値とに基づき状態Cの飽和液冷媒温度が周囲温度値よりも低くなるように電子式膨張弁130および開閉弁160の開度を計算し、電子式膨張弁130および開度調整部161にそれぞれの開度を指示する。
開度調整部161は、開閉弁160の開度を指示する信号を制御回路170から受信すると、指示された信号に基づき開閉弁160の開度を調整する。
The control circuit 170 opens the electronic expansion valve 130 and the on-off valve 160 so that the saturated liquid refrigerant temperature in the state C becomes lower than the ambient temperature value based on the refrigerant pressure value in the state C, the refrigerant temperature value, and the ambient temperature value. The degree is calculated, and the opening degree is instructed to the electronic expansion valve 130 and the opening degree adjusting unit 161.
When the opening adjustment unit 161 receives a signal indicating the opening of the on-off valve 160 from the control circuit 170, the opening adjusting unit 161 adjusts the opening of the on-off valve 160 based on the instructed signal.

以上のように本実施の形態5によれば、冷媒排出時に開閉弁160の開度も調整するので、電子式膨張弁130から開閉弁160までの冷媒圧力を、電子式膨張弁130のみを備えた場合よりも細かく制御することができる。   As described above, according to the fifth embodiment, since the opening degree of the on-off valve 160 is also adjusted when the refrigerant is discharged, the refrigerant pressure from the electronic expansion valve 130 to the on-off valve 160 is provided only with the electronic expansion valve 130. It is possible to control more finely than the case.

なお、上述では、制御回路170は冷媒圧力値と冷媒温度値と周囲温度値とに基づいて、電子式膨張弁130および開閉弁160の開度を調整する旨を説明した。しかし、制御回路170は、冷媒圧力値と周囲温度値とに基づき開度を調整したり、冷媒温度値と周囲温度値に基づき開度を調整したり、フィン142に設けた温度測定器301から取得したフィンの温度と周囲温度値に基づき開度を調整しても良い。   In the above description, it has been described that the control circuit 170 adjusts the opening degrees of the electronic expansion valve 130 and the on-off valve 160 based on the refrigerant pressure value, the refrigerant temperature value, and the ambient temperature value. However, the control circuit 170 adjusts the opening degree based on the refrigerant pressure value and the ambient temperature value, adjusts the opening degree based on the refrigerant temperature value and the ambient temperature value, or from the temperature measuring device 301 provided on the fin 142. The opening degree may be adjusted based on the acquired fin temperature and ambient temperature value.

実施の形態6.
図10は、本発明の実施の形態6に係る冷凍サイクル装置100の構成図である。図10に示す実施の形態6に係る冷凍サイクル装置100は、実施の形態4に係る冷凍サイクル装置100に蒸発器140に散水する散水器600を備えたものである。図8に示す実施の形態4に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 6 FIG.
FIG. 10 is a configuration diagram of a refrigeration cycle apparatus 100 according to Embodiment 6 of the present invention. A refrigeration cycle apparatus 100 according to Embodiment 6 shown in FIG. 10 is provided with a sprinkler 600 that sprinkles water on the evaporator 140 in the refrigeration cycle apparatus 100 according to Embodiment 4. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 4 shown in FIG. 8, and the description is abbreviate | omitted.

制御回路170は、冷媒排出開始信号が与えられると、散水器600に散水の開始を指示する散水開始信号を散水器600に出力する。冷媒排出が終了した旨を検知すると、散水の終了を指示する散水終了信号を散水器600に出力する。また、電子式膨張弁130を調整するのに伴い、散水量も計算して散水器600に指示しても良い。   When the refrigerant discharge start signal is given, the control circuit 170 outputs a sprinkling start signal that instructs the sprinkler 600 to start sprinkling. When it is detected that the refrigerant discharge has ended, a sprinkling end signal instructing the end of sprinkling is output to the sprinkler 600. Further, as the electronic expansion valve 130 is adjusted, the watering amount may be calculated and instructed to the watering device 600.

散水器600は、制御回路170からの指示に基づき、蒸発器140のフィン142に散水するものである。散水される水は、散水器600が備えるタンクに貯水されていた水であったり、外部から供給されるものであったりする。   The sprinkler 600 sprinkles water on the fins 142 of the evaporator 140 based on instructions from the control circuit 170. The water to be sprinkled may be water stored in a tank provided in the sprinkler 600 or supplied from the outside.

次に、冷媒排出時の蒸発器140について説明する。
冷媒排出時、電子式膨張弁130の開度が調整されて、蒸発器140において冷媒が熱交換するので、蒸発器140、特にフィン142の温度は、冷媒排出前に比べて低下する。ここで、蒸発器140の温度が冷凍サイクル装置100の周囲の空気が露点よりも低くなると、蒸発器140に結露が発生する。冷媒の蒸発量によっては、結露して蒸発器140に付着した水分は冷やされて霜となる。これらの結露水や着霜より、蒸発器140の冷却量は増加する。特に、本実施の形態6では、冷媒放出時に蒸発器140が散水器600から散水されるので、散水しない場合よりも蒸発器140に付着する水分や着霜量が増加するとともに、蒸発器140の冷却量も増加する。
Next, the evaporator 140 at the time of refrigerant discharge will be described.
When the refrigerant is discharged, the opening degree of the electronic expansion valve 130 is adjusted, and the refrigerant exchanges heat in the evaporator 140. Therefore, the temperature of the evaporator 140, particularly the fin 142, is lower than before the refrigerant is discharged. Here, when the temperature of the evaporator 140 becomes lower than the dew point of the air around the refrigeration cycle apparatus 100, condensation occurs in the evaporator 140. Depending on the evaporation amount of the refrigerant, the moisture that has condensed and adhered to the evaporator 140 is cooled to become frost. The amount of cooling of the evaporator 140 increases due to the condensed water and frost formation. In particular, in the sixth embodiment, since the evaporator 140 is sprinkled from the water sprinkler 600 when the refrigerant is discharged, the amount of water and frost that adheres to the evaporator 140 is increased as compared with the case where the water is not sprinkled. The amount of cooling also increases.

蒸発器140に付着した氷や水分には、潜熱としての蓄熱がされるので、の冷却量が増加するので、蒸発器140は冷媒封入時に封入された冷媒もさらに冷却でき、冷媒の超臨界状態への状態変化を抑制することができる。   Since ice and water adhering to the evaporator 140 are stored as latent heat, the amount of cooling increases, so the evaporator 140 can further cool the refrigerant enclosed when the refrigerant is sealed, and the refrigerant is in a supercritical state. It is possible to suppress a change in state.

以上のように、本実施の形態6によれば、蒸発器140は、冷媒排出時に散水されることで、蓄積する冷却量が増加するので、冷媒封入時に流入した冷媒を冷却して冷媒の封入を促進することができる。   As described above, according to the sixth embodiment, the evaporator 140 is sprinkled with water when the refrigerant is discharged, so that the accumulated cooling amount increases. Can be promoted.

ところで、上述では、電子式膨張弁130の開度を調整する際に、蒸発器140に散水する場合について説明した。しかし、電子式膨張弁130だけでなく開閉弁160の開度も調整する場合にも、蒸発器140に散水しても良い。特に、電子式膨張弁130の開度および開閉弁160の開度を調整するのに伴い、散水量を調整すれば、蒸発器140を効率的に冷却することができる。   By the way, in the above, the case where water was sprayed to the evaporator 140 when the opening degree of the electronic expansion valve 130 was adjusted was described. However, when adjusting not only the electronic expansion valve 130 but also the opening / closing valve 160, the evaporator 140 may be sprinkled. In particular, the evaporator 140 can be efficiently cooled if the amount of water spray is adjusted as the opening degree of the electronic expansion valve 130 and the opening degree of the on-off valve 160 are adjusted.

実施の形態7.
図11は、本実施の形態7に係る冷凍サイクル装置100の構成図である。図11に示す実施の形態7に係る冷凍サイクル装置100は、実施の形態1に係る冷凍サイクル装置100に蓄熱用熱交換器700および蓄熱用熱交換器700の蓄熱材の温度を測定する蓄熱材温度測定器701を設けたものである。図1に示す実施の形態1に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 7 FIG.
FIG. 11 is a configuration diagram of the refrigeration cycle apparatus 100 according to the seventh embodiment. The refrigeration cycle apparatus 100 according to the seventh embodiment shown in FIG. 11 is a heat storage material that measures the temperature of the heat storage heat exchanger 700 and the heat storage material of the heat storage heat exchanger 700 in the refrigeration cycle apparatus 100 according to the first embodiment. A temperature measuring device 701 is provided. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on Embodiment 1 shown in FIG. 1, and the description is abbreviate | omitted.

図12は、蓄熱用熱交換器700の構成を示す図である。図12(a)は図11と同じ方向から見た断面図、図12(b)は図12(a)のX−X’断面図である。蓄熱用熱交換器700は、容器702の中に蓄熱材703が充填されており、この容器の中を循環回路を形成する冷媒配管704が貫通するものである。蓄熱材703は、水や空気、その他蓄熱できる媒体であれば材料を問わない。   FIG. 12 is a diagram illustrating a configuration of the heat storage heat exchanger 700. 12A is a cross-sectional view seen from the same direction as FIG. 11, and FIG. 12B is an X-X ′ cross-sectional view of FIG. In the heat storage heat exchanger 700, a heat storage material 703 is filled in a container 702, and a refrigerant pipe 704 that forms a circulation circuit passes through the container 702. The heat storage material 703 may be any material as long as it is water, air, or other medium capable of storing heat.

次に冷媒排出時の冷凍サイクル装置100について説明する。
冷媒排出時、状態Aであった冷媒は電子式膨張弁130で減圧し、状態Bになる。その後、冷媒は蓄熱用熱交換器700と熱交換して蓄熱材703を冷却する。冷媒は、さらに蒸発器140を通過して最終的に状態Cとなり、開閉弁160から循環回路の外に排出される。
なお、制御回路170は、蓄熱材温度測定器701が測定した蓄熱材703の温度に基づき、電子式膨張弁130の開度を調整する。
Next, the refrigeration cycle apparatus 100 when the refrigerant is discharged will be described.
When the refrigerant is discharged, the refrigerant in the state A is decompressed by the electronic expansion valve 130 and becomes the state B. Thereafter, the refrigerant exchanges heat with the heat storage heat exchanger 700 to cool the heat storage material 703. The refrigerant further passes through the evaporator 140 and finally enters the state C, and is discharged from the on-off valve 160 to the outside of the circulation circuit.
The control circuit 170 adjusts the opening degree of the electronic expansion valve 130 based on the temperature of the heat storage material 703 measured by the heat storage material temperature measuring device 701.

蓄熱材703は冷却されているため、封入された冷媒が冷媒配管704を通過すると、冷却されて気液二相状態や液相状態になり、圧力の上昇が抑制される。これにより、ボンベから冷凍サイクル装置への冷媒の流入が促進される。
なお、蓄熱材703の熱容量や電子式膨張弁130の開度の調整によっては、冷媒排出時に、蓄熱用熱交換器700だけでなく蒸発器140も冷却される。蒸発器140も冷却されている場合には、封入された冷媒は、蒸発器140および蓄熱用熱交換器700を通過した際に冷却される。
Since the heat storage material 703 is cooled, when the enclosed refrigerant passes through the refrigerant pipe 704, the heat storage material 703 is cooled to be in a gas-liquid two-phase state or a liquid phase state, and an increase in pressure is suppressed. Thereby, the inflow of the refrigerant from the cylinder to the refrigeration cycle apparatus is promoted.
Depending on the adjustment of the heat capacity of the heat storage material 703 and the opening of the electronic expansion valve 130, not only the heat storage heat exchanger 700 but also the evaporator 140 is cooled when the refrigerant is discharged. When the evaporator 140 is also cooled, the enclosed refrigerant is cooled when it passes through the evaporator 140 and the heat storage heat exchanger 700.

以上のように、本実施の形態7によれば、冷媒排出時に蒸発器140だけでなく蓄熱用熱交換器700も冷却するので、冷媒封入時の冷媒冷却を強化して冷媒の封入を促進することができる。   As described above, according to the seventh embodiment, not only the evaporator 140 but also the heat storage heat exchanger 700 is cooled when the refrigerant is discharged, so that the cooling of the refrigerant at the time of charging the refrigerant is enhanced to facilitate the charging of the refrigerant. be able to.

ところで、上述では、冷媒排出時の電子式膨張弁130を蓄熱材703が所定温度よりも低くなるよう調整する旨について説明した。しかし、蒸発器140から流出した冷媒の圧力や温度、蒸発器140のフィン142の温度なども参照して電子式膨張弁130の開度を調整しても良い。また、冷媒排出時に電子式膨張弁130だけでなく、開閉弁調整部161を介して開閉弁160の開度を調整しても良い。   In the above description, the electronic expansion valve 130 during refrigerant discharge is adjusted so that the heat storage material 703 is lower than a predetermined temperature. However, the opening degree of the electronic expansion valve 130 may be adjusted with reference to the pressure and temperature of the refrigerant flowing out of the evaporator 140 and the temperature of the fin 142 of the evaporator 140. Further, the opening degree of the on-off valve 160 may be adjusted not only through the electronic expansion valve 130 but also through the on-off valve adjusting unit 161 when the refrigerant is discharged.

また、上述においては、蓄熱用熱交換器700を電子式膨張弁130と蒸発器140との間に設けた。しかし、蒸発器140と開閉弁160との間に設け、冷媒排出時には蒸発器140および蓄熱用熱交換器700を冷却するように電子式膨張弁130の開度を調整しても良い。   In the above description, the heat storage heat exchanger 700 is provided between the electronic expansion valve 130 and the evaporator 140. However, the opening degree of the electronic expansion valve 130 may be adjusted between the evaporator 140 and the on-off valve 160 so that the evaporator 140 and the heat storage heat exchanger 700 are cooled when the refrigerant is discharged.

実施の形態8.
実施の形態1から7では、冷媒排出時に主に蒸発器140や蓄熱用熱交換機700を冷却する場合について説明した。本実施の形態8では、主に給湯用の水を冷却する場合について説明する。
図13は、本実施の形態8に係る冷凍サイクル装置100の構成図である。図13に示す実施の形態8に係る冷凍サイクル装置100は、冷媒を排出したり封入したりする開閉弁160を圧縮機110とガスクーラ120との間に設けたものである。図1に示す本実施の形態1に係る冷凍サイクル装置100と同一の構成には同一の符号を付し、その説明は省略する。
Embodiment 8 FIG.
In the first to seventh embodiments, the case where the evaporator 140 and the heat storage heat exchanger 700 are mainly cooled when the refrigerant is discharged has been described. In the eighth embodiment, a case where water for hot water supply is mainly cooled will be described.
FIG. 13 is a configuration diagram of the refrigeration cycle apparatus 100 according to the eighth embodiment. In the refrigeration cycle apparatus 100 according to Embodiment 8 shown in FIG. 13, an on-off valve 160 that discharges and encloses the refrigerant is provided between the compressor 110 and the gas cooler 120. The same code | symbol is attached | subjected to the structure same as the refrigerating-cycle apparatus 100 which concerns on this Embodiment 1 shown in FIG. 1, and the description is abbreviate | omitted.

図13において、冷媒圧力検出器200および冷媒温度検出器300はガスクーラ120と開閉弁160との間に設けられている。また、ガスクーラ120は、給湯用の配水管801やタンク802を備え、ガスクーラ120の筐体内では循環回路の冷媒と配水管801内の水とが熱交換する。さらに、配水管801やタンク802にはバルブ803および804が設けられ、バルブの開閉により給水元や給水先との水の流入出を制御する。また、給水温度測定器805が配水管801のガスクーラ120への入口部に設けられ、水温度を測定する。
なお、図13では図示しないが、制御回路170と、冷媒圧力測定器200、冷媒温度測定器300、給水温度測定器805、バルブ802およびバルブ803とは接続されており、制御回路170と各装置とは測定値や制御指令を送受信する。
In FIG. 13, the refrigerant pressure detector 200 and the refrigerant temperature detector 300 are provided between the gas cooler 120 and the on-off valve 160. Further, the gas cooler 120 includes a water distribution pipe 801 and a tank 802 for hot water supply, and heat is exchanged between the refrigerant in the circulation circuit and the water in the water distribution pipe 801 in the casing of the gas cooler 120. Furthermore, valves 803 and 804 are provided in the water distribution pipe 801 and the tank 802, and the flow of water to and from the water supply source and the water supply destination is controlled by opening and closing the valves. Further, a water supply temperature measuring device 805 is provided at the inlet of the water distribution pipe 801 to the gas cooler 120 to measure the water temperature.
Although not shown in FIG. 13, the control circuit 170, the refrigerant pressure measuring device 200, the refrigerant temperature measuring device 300, the feed water temperature measuring device 805, the valve 802 and the valve 803 are connected, and the control circuit 170 and each device are connected. Transmits and receives measured values and control commands.

図14は、本実施の形態8に係るガスクーラ120の構成図である。図14(a)はガスクーラ120の冷媒配管121を示す図であり、図14(b)は冷媒配管121の断面を示す図である。
冷媒配管121はガスクーラ120の中で螺旋状に配管されており、水配管801はガスクーラ120の冷媒配管121の周りに密着して、水配管801とともに螺旋状に配管されている。
FIG. 14 is a configuration diagram of the gas cooler 120 according to the eighth embodiment. FIG. 14A is a view showing the refrigerant pipe 121 of the gas cooler 120, and FIG. 14B is a view showing a cross section of the refrigerant pipe 121.
The refrigerant pipe 121 is spirally piped in the gas cooler 120, and the water pipe 801 is closely attached around the refrigerant pipe 121 of the gas cooler 120 and is spirally piped together with the water pipe 801.

制御回路170は、冷媒排出開始信号が入力されると、バルブ803および804を閉じ、給湯用の水はバルブ803からバルブ804までの間の配水管801やタンク802に滞留する。また、制御回路170は、給水温度測定器805から水温度値を、冷媒圧力測定器200から冷媒圧力値を、冷媒温度測定器300から冷媒温度値を取得し、これらの値に基づき、電子式膨張弁103の開度を調整する。冷媒排出時の冷媒と水との熱交換により、ガスクーラ120内の水温度は、周囲温度に対し所定温度低くなる。   When the refrigerant discharge start signal is input, the control circuit 170 closes the valves 803 and 804, and hot water supply water stays in the water distribution pipe 801 and the tank 802 between the valve 803 and the valve 804. In addition, the control circuit 170 acquires the water temperature value from the feed water temperature measuring device 805, the refrigerant pressure value from the refrigerant pressure measuring device 200, and the refrigerant temperature value from the refrigerant temperature measuring device 300, and based on these values, the electronic circuit The opening degree of the expansion valve 103 is adjusted. Due to the heat exchange between the refrigerant and water when the refrigerant is discharged, the water temperature in the gas cooler 120 becomes lower than the ambient temperature by a predetermined temperature.

水配管801やタンク802に滞留した水は、ガスクーラ120を通過する冷媒と熱交換し、冷却される。制御回路170は、水温度値、冷媒温度値、冷媒圧力値等に加え、滞留する水の量も参照して、電子式膨張弁103の開度や開閉弁160の開度を調整しても良い。   The water staying in the water pipe 801 and the tank 802 is cooled by exchanging heat with the refrigerant passing through the gas cooler 120. The control circuit 170 adjusts the opening degree of the electronic expansion valve 103 and the opening / closing valve 160 with reference to the water temperature value, the refrigerant temperature value, the refrigerant pressure value, and the like, as well as the amount of remaining water. good.

次に、冷媒を封入する場合について説明する。冷媒は、開閉弁160から冷媒が封入されると、圧縮機110と、ガスクーラ120に向かって流れる。ガスクーラ120を通過する冷媒は、水配管801やタンク802に滞留した水に冷却される。すると、実施の形態1〜7と同様、冷媒圧力の上昇が抑制されるので、冷媒の封入が促進される。   Next, a case where a refrigerant is sealed will be described. When the refrigerant is sealed from the on-off valve 160, the refrigerant flows toward the compressor 110 and the gas cooler 120. The refrigerant that passes through the gas cooler 120 is cooled by the water retained in the water pipe 801 and the tank 802. Then, since the raise of a refrigerant pressure is suppressed like Embodiment 1-7, enclosure of a refrigerant | coolant is accelerated | stimulated.

以上のように、実施の形態8によれば、冷媒排出時に、排出される冷媒をガスクーラ120で蒸発させることで、ガスクーラ120で熱交換される水を冷却できるので、冷媒封入時に、流入した冷媒を冷却できる。よって、実施の形態1等と同様、冷媒封入時に冷媒の圧力上昇を抑制できるため、冷媒封入を促進することができる。   As described above, according to the eighth embodiment, when the refrigerant is discharged, the discharged refrigerant is evaporated by the gas cooler 120 so that the water exchanged by the gas cooler 120 can be cooled. Can be cooled. Therefore, similarly to Embodiment 1 and the like, since the increase in the pressure of the refrigerant can be suppressed when the refrigerant is sealed, the refrigerant filling can be promoted.

本発明の実施の形態1に係る冷凍サイクル装置の構成図である。1 is a configuration diagram of a refrigeration cycle apparatus according to Embodiment 1 of the present invention. 本発明の実施の形態1に係る蒸発器104の構成図である。It is a block diagram of the evaporator 104 which concerns on Embodiment 1 of this invention. 本発明の実施の形態1において冷媒を排出する際の冷媒の状態変化図である。It is a state change figure of a refrigerant at the time of discharging a refrigerant in Embodiment 1 of the present invention. 本発明の実施の形態1において冷媒を封入する際の冷媒の状態変化図である。It is a state change figure of a refrigerant at the time of enclosing a refrigerant in Embodiment 1 of the present invention. 本発明の実施の形態2に係る冷凍サイクル装置の構成図である。It is a block diagram of the refrigeration cycle apparatus which concerns on Embodiment 2 of this invention. 本発明の実施の形態3に係る冷凍サイクル装置の構成図である。It is a block diagram of the refrigerating-cycle apparatus which concerns on Embodiment 3 of this invention. 本発明の実施の形態3に係る蒸発器104の構成図である。It is a block diagram of the evaporator 104 which concerns on Embodiment 3 of this invention. 本発明の実施の形態4に係る冷凍サイクル装置100の構成図である。It is a block diagram of the refrigerating-cycle apparatus 100 which concerns on Embodiment 4 of this invention. 本発明の実施の形態5に係る冷凍サイクル装置100の構成図である。It is a block diagram of the refrigerating cycle apparatus 100 which concerns on Embodiment 5 of this invention. 本発明の実施の形態6に係る冷凍サイクル装置100の構成図である。It is a block diagram of the refrigerating cycle apparatus 100 which concerns on Embodiment 6 of this invention. 本発明の実施の形態7に係る冷凍サイクル装置100の構成図である。It is a block diagram of the refrigerating-cycle apparatus 100 which concerns on Embodiment 7 of this invention. 本発明の実施の形態7に係る蓄熱用熱交換機700の構成図である。It is a block diagram of the heat exchanger 700 for heat storage which concerns on Embodiment 7 of this invention. 本発明の実施の形態8に係る冷凍サイクル装置100の構成図である。It is a block diagram of the refrigerating-cycle apparatus 100 which concerns on Embodiment 8 of this invention. 本発明の実施の形態8に係るガスクーラ120の構成図である。It is a block diagram of the gas cooler 120 which concerns on Embodiment 8 of this invention. 従来の冷凍サイクル装置において冷媒を封入する際の冷媒の状態変化を説明する図である。It is a figure explaining the state change of the refrigerant | coolant at the time of enclosing a refrigerant | coolant in the conventional refrigeration cycle apparatus.

符号の説明Explanation of symbols

100 冷凍サイクル装置、110 圧縮機、120 ガスクーラ、130 電子式膨張弁、140 蒸発器、142 フィン、160 開閉弁、161 開閉弁制御部、170 制御回路、180 周囲温度測定器、200 冷媒圧力測定器、300 冷媒温度測定器、600 散水器、700 蓄熱用熱交換器、701 蓄熱材温度測定器、801 配水管、802 タンク、803バルブ、804 バルブ   DESCRIPTION OF SYMBOLS 100 Refrigeration cycle apparatus, 110 Compressor, 120 Gas cooler, 130 Electronic expansion valve, 140 Evaporator, 142 Fin, 160 On-off valve, 161 On-off valve control part, 170 Control circuit, 180 Ambient temperature measuring device, 200 Refrigerant pressure measuring device , 300 Refrigerant temperature measuring device, 600 Sprinkler, 700 Heat storage heat exchanger, 701 Heat storage material temperature measuring device, 801 Water distribution pipe, 802 Tank, 803 valve, 804 valve

Claims (10)

流入した冷媒を圧縮して吐出する圧縮機と、
前記圧縮機が吐出した前記冷媒を凝縮させる凝縮器と、
前記凝縮器からの前記冷媒を膨張させる膨張弁と、
前記膨張弁からの前記冷媒を蒸発させて前記圧縮機に流入させる蒸発器とを備えた循環回路、
前記蒸発器と前記圧縮機との間に設けられ、前記循環回路と外部とを連通させる開閉弁、
前記開閉弁を開く場合に前記膨張弁の開度を制御する制御回路、
を備えた冷凍サイクル装置。
A compressor that compresses and discharges the refrigerant flowing in;
A condenser for condensing the refrigerant discharged from the compressor;
An expansion valve for expanding the refrigerant from the condenser;
A circulation circuit comprising an evaporator for evaporating the refrigerant from the expansion valve and allowing the refrigerant to flow into the compressor;
An on-off valve provided between the evaporator and the compressor, which communicates the circulation circuit with the outside;
A control circuit for controlling the opening of the expansion valve when the on-off valve is opened;
A refrigeration cycle apparatus comprising:
周囲温度を測定する周囲温度測定器を備え、
制御回路は、前記周囲温度測定器が測定した前記周囲温度に基づき膨張弁の開度を調整することを特徴とする請求項1記載の冷凍サイクル装置。
Equipped with an ambient temperature measuring device to measure the ambient temperature,
The refrigeration cycle apparatus according to claim 1, wherein the control circuit adjusts an opening degree of the expansion valve based on the ambient temperature measured by the ambient temperature measuring device.
蒸発器と開閉弁との間に設けられて冷媒の圧力を測定する冷媒圧力測定器を備え、
制御回路は、周囲温度測定器が測定した周囲温度および前記冷媒圧力測定器が測定した前記圧力に基づき膨張弁の開度を調整することを特徴とする請求項2記載の冷凍サイクル装置。
A refrigerant pressure measuring device is provided between the evaporator and the on-off valve to measure the pressure of the refrigerant,
3. The refrigeration cycle apparatus according to claim 2, wherein the control circuit adjusts the opening of the expansion valve based on the ambient temperature measured by the ambient temperature measuring device and the pressure measured by the refrigerant pressure measuring device.
蒸発器と開閉弁との間に設けられて冷媒の温度を測定する冷媒温度測定器を備え、
制御回路は、周囲温度測定器が測定した周囲温度および前記冷媒温度測定器が測定した前記温度に基づき膨張弁の開度を調整することを特徴とする請求項2記載の冷凍サイクル装置。
A refrigerant temperature measuring device is provided between the evaporator and the on-off valve to measure the temperature of the refrigerant,
The refrigeration cycle apparatus according to claim 2, wherein the control circuit adjusts the opening of the expansion valve based on the ambient temperature measured by the ambient temperature measuring device and the temperature measured by the refrigerant temperature measuring device.
蒸発器はフィンを備え、
前記フィンは、前記フィンの温度を測定するフィン温度測定器を備え、
制御回路は、周囲温度測定器が測定した周囲温度および前記フィン温度測定器が測定した前記温度に基づき膨張弁の開度を調整することを特徴とする請求項2記載の冷凍サイクル装置。
The evaporator is equipped with fins,
The fin includes a fin temperature measuring device for measuring the temperature of the fin,
3. The refrigeration cycle apparatus according to claim 2, wherein the control circuit adjusts the opening of the expansion valve based on the ambient temperature measured by the ambient temperature measuring device and the temperature measured by the fin temperature measuring device.
散水開始および散水終了の指示に従い蒸発器に散水する散水器を備え、
制御回路は、開閉弁を開く場合に散水開始の指示を前記散水器に与え、開閉弁を閉じる場合に散水終了の指示を前記散水器に与えることを特徴とする請求項2記載の冷凍サイクル装置。
A sprinkler for sprinkling water on the evaporator according to the instructions to start and end the sprinkling,
The refrigeration cycle apparatus according to claim 2, wherein the control circuit gives an instruction to start watering to the watering device when the on-off valve is opened, and gives an instruction to end the watering to the watering device when the on-off valve is closed. .
制御回路は、膨張弁の開度に基づき散水量を計算して散水器に指示し、
散水器は、前記制御回路から指示された散水量で散水することを特徴とする請求項7記載の冷凍サイクル装置。
The control circuit calculates the watering amount based on the opening of the expansion valve and instructs the watering device,
The refrigeration cycle apparatus according to claim 7, wherein the sprinkler sprinkles with a sprinkling amount instructed from the control circuit.
膨張弁と開閉弁との間であって前記膨張弁の下流に設けられ、冷媒と熱交換する蓄熱材を備えた蓄熱器を備えた請求項2記載の冷凍サイクル装置。 The refrigeration cycle apparatus according to claim 2, further comprising a heat accumulator that is provided between the expansion valve and the on-off valve and downstream of the expansion valve and includes a heat storage material that exchanges heat with the refrigerant. 制御回路は、周囲温度測定器が測定した周囲温度に基づき膨張弁および開閉弁の開度を計算し、前記開度を前記膨張弁および前記開閉弁に指示し、
前記膨張弁および前記開閉弁は、前記制御回路から指示された開度で開くことを特徴とする請求項2記載の冷凍サイクル装置。
The control circuit calculates the opening degree of the expansion valve and the on-off valve based on the ambient temperature measured by the ambient temperature measuring device, and instructs the opening degree to the expansion valve and the on-off valve,
The refrigeration cycle apparatus according to claim 2, wherein the expansion valve and the on-off valve are opened at an opening degree instructed by the control circuit.
流入した冷媒を圧縮して吐出する圧縮機と、
前記圧縮機が吐出した前記冷媒を凝縮させるガスクーラと、
前記ガスクーラからの前記冷媒を膨張させる膨張弁と、
前記膨張弁からの前記冷媒を蒸発させて前記圧縮機に流入させる蒸発器とを備えた循環回路、
前記圧縮機と前記ガスクーラとの間に設けられて、前記循環回路と外部とを連通させる開閉弁、
前記開閉弁を開く場合に前記膨張弁の開度を制御する制御回路、
を備えた冷凍サイクル装置。
A compressor that compresses and discharges the refrigerant flowing in;
A gas cooler for condensing the refrigerant discharged from the compressor;
An expansion valve for expanding the refrigerant from the gas cooler;
A circulation circuit comprising an evaporator for evaporating the refrigerant from the expansion valve and allowing the refrigerant to flow into the compressor;
An on-off valve provided between the compressor and the gas cooler for communicating the circulation circuit with the outside;
A control circuit for controlling the opening of the expansion valve when the on-off valve is opened;
A refrigeration cycle apparatus comprising:
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012145254A (en) * 2011-01-11 2012-08-02 Mitsubishi Electric Corp Refrigeration cycle device and refrigerant discharge device
WO2013156027A1 (en) * 2012-04-17 2013-10-24 Danfoss A/S A controller for a vapour compression system and a method for controlling a vapour compression system
FR2999691A1 (en) * 2012-12-19 2014-06-20 Valeo Systemes Thermiques SYSTEM FOR ELECTRICALLY REGULATING A RELAXATION OF A REFRIGERANT FLUID AND METHOD FOR CONTROLLING SUCH A SYSTEM
JP2019214542A (en) * 2018-06-14 2019-12-19 Jnc株式会社 MANUFACTURING METHOD OF β-HYDROXYLACTONE (METH)ACRYLIC ACID ESTER
JP2020071002A (en) * 2018-11-01 2020-05-07 株式会社長府製作所 Heat pump device

Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6325455A (en) * 1986-07-18 1988-02-02 株式会社日立製作所 Refrigeration system
JPS646650A (en) * 1987-06-26 1989-01-11 Yamato Setsubi Koji Kk Refrigerating method
JPH0468983U (en) * 1990-10-24 1992-06-18
JPH04208628A (en) * 1990-09-28 1992-07-30 Mitsubishi Heavy Ind Ltd Air conditioning system for magnetic levitation rolling stock
JPH05164437A (en) * 1991-12-12 1993-06-29 Hitachi Ltd Air conditioner
JPH05288439A (en) * 1992-04-03 1993-11-02 Daikin Ind Ltd Refrigerating plant
JPH0674622A (en) * 1992-08-27 1994-03-18 Zexel Corp Refrigerant charging method
JPH06323639A (en) * 1993-05-10 1994-11-25 Hitachi Ltd Method for controlling chilled water supplying device
JPH08200917A (en) * 1995-01-20 1996-08-09 Sanyo Electric Co Ltd Cooler for vending machine
JPH08254376A (en) * 1995-03-17 1996-10-01 Mitsubishi Electric Corp Air conditioner
JPH08324232A (en) * 1995-05-30 1996-12-10 Mitsubishi Heavy Ind Ltd Control device of vehicular air conditioner
JPH10311614A (en) * 1997-05-13 1998-11-24 Fuji Electric Co Ltd Heat storage type cooling device
JP2001071741A (en) * 1999-09-02 2001-03-21 Zexel Valeo Climate Control Corp Air conditioning device for vehicle
JP2002054834A (en) * 2000-08-08 2002-02-20 Mitsubishi Electric Corp Refrigerating cycle device
JP2002098425A (en) * 2000-09-21 2002-04-05 Toshiba Kyaria Kk Refrigerating cycle device
JP2002372346A (en) * 2001-06-13 2002-12-26 Daikin Ind Ltd Refrigerant circuit, its operation checking method, method for filling refrigerant, and closing valve for filling refrigerant
JP2004019884A (en) * 2002-06-19 2004-01-22 Mitsubishi Electric Building Techno Service Co Ltd Refrigerant cylinder
JP2005291679A (en) * 2004-04-06 2005-10-20 Tgk Co Ltd Refrigerating system

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6325455A (en) * 1986-07-18 1988-02-02 株式会社日立製作所 Refrigeration system
JPS646650A (en) * 1987-06-26 1989-01-11 Yamato Setsubi Koji Kk Refrigerating method
JPH04208628A (en) * 1990-09-28 1992-07-30 Mitsubishi Heavy Ind Ltd Air conditioning system for magnetic levitation rolling stock
JPH0468983U (en) * 1990-10-24 1992-06-18
JPH05164437A (en) * 1991-12-12 1993-06-29 Hitachi Ltd Air conditioner
JPH05288439A (en) * 1992-04-03 1993-11-02 Daikin Ind Ltd Refrigerating plant
JPH0674622A (en) * 1992-08-27 1994-03-18 Zexel Corp Refrigerant charging method
JPH06323639A (en) * 1993-05-10 1994-11-25 Hitachi Ltd Method for controlling chilled water supplying device
JPH08200917A (en) * 1995-01-20 1996-08-09 Sanyo Electric Co Ltd Cooler for vending machine
JPH08254376A (en) * 1995-03-17 1996-10-01 Mitsubishi Electric Corp Air conditioner
JPH08324232A (en) * 1995-05-30 1996-12-10 Mitsubishi Heavy Ind Ltd Control device of vehicular air conditioner
JPH10311614A (en) * 1997-05-13 1998-11-24 Fuji Electric Co Ltd Heat storage type cooling device
JP2001071741A (en) * 1999-09-02 2001-03-21 Zexel Valeo Climate Control Corp Air conditioning device for vehicle
JP2002054834A (en) * 2000-08-08 2002-02-20 Mitsubishi Electric Corp Refrigerating cycle device
JP2002098425A (en) * 2000-09-21 2002-04-05 Toshiba Kyaria Kk Refrigerating cycle device
JP2002372346A (en) * 2001-06-13 2002-12-26 Daikin Ind Ltd Refrigerant circuit, its operation checking method, method for filling refrigerant, and closing valve for filling refrigerant
JP2004019884A (en) * 2002-06-19 2004-01-22 Mitsubishi Electric Building Techno Service Co Ltd Refrigerant cylinder
JP2005291679A (en) * 2004-04-06 2005-10-20 Tgk Co Ltd Refrigerating system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012145254A (en) * 2011-01-11 2012-08-02 Mitsubishi Electric Corp Refrigeration cycle device and refrigerant discharge device
WO2013156027A1 (en) * 2012-04-17 2013-10-24 Danfoss A/S A controller for a vapour compression system and a method for controlling a vapour compression system
CN104321599A (en) * 2012-04-17 2015-01-28 丹佛斯公司 A controller for a vapour compression system and a method for controlling a vapour compression system
US10359222B2 (en) 2012-04-17 2019-07-23 Danfoss A/S Controller for a vapour compression system and a method for controlling a vapour compression system
FR2999691A1 (en) * 2012-12-19 2014-06-20 Valeo Systemes Thermiques SYSTEM FOR ELECTRICALLY REGULATING A RELAXATION OF A REFRIGERANT FLUID AND METHOD FOR CONTROLLING SUCH A SYSTEM
WO2014095591A1 (en) * 2012-12-19 2014-06-26 Valeo Systemes Thermiques System for the electrical regulation of the expansion of a coolant and method for controlling such a system
JP2019214542A (en) * 2018-06-14 2019-12-19 Jnc株式会社 MANUFACTURING METHOD OF β-HYDROXYLACTONE (METH)ACRYLIC ACID ESTER
JP2020071002A (en) * 2018-11-01 2020-05-07 株式会社長府製作所 Heat pump device

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