JPH0833242B2 - Refrigeration equipment - Google Patents

Refrigeration equipment

Info

Publication number
JPH0833242B2
JPH0833242B2 JP62090514A JP9051487A JPH0833242B2 JP H0833242 B2 JPH0833242 B2 JP H0833242B2 JP 62090514 A JP62090514 A JP 62090514A JP 9051487 A JP9051487 A JP 9051487A JP H0833242 B2 JPH0833242 B2 JP H0833242B2
Authority
JP
Japan
Prior art keywords
temperature
refrigerant
cooled
medium
evaporator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP62090514A
Other languages
Japanese (ja)
Other versions
JPS63259353A (en
Inventor
進司 佐藤
広志 小川
信博 舟橋
敏雄 山下
寛爾 不殿
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP62090514A priority Critical patent/JPH0833242B2/en
Publication of JPS63259353A publication Critical patent/JPS63259353A/en
Publication of JPH0833242B2 publication Critical patent/JPH0833242B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Air Conditioning Control Device (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は空気調和機、冷水機、冷凍機等の冷凍装置に
関する。
TECHNICAL FIELD The present invention relates to a refrigerating device such as an air conditioner, a chiller, a refrigerator, or the like.

(従来の技術) 従来の空気調和機の冷媒回路の1例が第6図に示さ
れ、圧縮機1から吐出された冷媒ガスは凝縮器2で冷却
されて凝縮液化し、次いで、電子式膨張弁3で減圧され
て断熱膨張し、次いで、蒸発器4でこれを流過する室内
に空気から吸熱することにより蒸発気化して圧縮機1に
戻る。
(Prior Art) An example of a refrigerant circuit of a conventional air conditioner is shown in FIG. 6, in which a refrigerant gas discharged from a compressor 1 is cooled by a condenser 2 to be condensed and liquefied, and then an electronic expansion is performed. It is decompressed by the valve 3 and adiabatically expanded. Then, the evaporator 4 evaporates and vaporizes by absorbing heat from the air in the chamber flowing through the evaporator 4 and returns to the compressor 1.

蒸発器4の出口における冷媒温度が冷媒温度検出器5
で検出され、蒸発器4出口における冷媒圧力は冷媒圧力
検出器6で検出され、これら検出器5及び6からの信号
を受けた制御装置7の出力によって電子式膨張弁3の開
度を制御し、これを通る冷媒流量を加減する。
The refrigerant temperature at the outlet of the evaporator 4 is the refrigerant temperature detector 5
The refrigerant pressure at the outlet of the evaporator 4 is detected by the refrigerant pressure detector 6, and the opening of the electronic expansion valve 3 is controlled by the output of the control device 7 which receives signals from these detectors 5 and 6. , The flow rate of the refrigerant passing through this is adjusted.

かくして、蒸発器4の出口における冷媒温度が蒸発器
4の出口における冷媒圧力に対応する飽和温度より約5d
eg位過熱され、蒸発器4の全能力が発揮される。
Thus, the refrigerant temperature at the outlet of the evaporator 4 is about 5d below the saturation temperature corresponding to the refrigerant pressure at the outlet of the evaporator 4.
For example, it is overheated and the full capacity of the evaporator 4 is exerted.

この冷凍装置をその冷凍能力以下の部分的冷凍能力で
運転する場合、即ち、冷凍能力制御運転時には圧縮機1
から吐出された冷媒ガスは凝縮器2及び電子式膨張弁3
をバイパスするバイパス回路10及び電子式調整弁11を経
て電子式膨張弁3を出た冷媒に合流する。
When operating this refrigerating apparatus with a partial refrigerating capacity equal to or lower than the refrigerating capacity, that is, during the refrigerating capacity control operation, the compressor 1
The refrigerant gas discharged from the condenser 2 and the electronic expansion valve 3
Via the bypass circuit 10 and the electronic control valve 11 for bypassing the refrigerant.

蒸発器4を流過した吹出空気温度は空気温度検出器8
で検出され、この信号は制御装置7に入力されてここで
温度設定器9で設定された設定温度の差が演算される。
そして、この制御装置7からの出力によって電子式調整
弁11が制御され、吹出空気温度が設定温度になるように
電子式調整弁11を通る冷媒量が加減される。
The temperature of the air blown through the evaporator 4 is measured by the air temperature detector 8
This signal is input to the controller 7 and the difference between the set temperatures set by the temperature setter 9 is calculated.
Then, the electronic control valve 11 is controlled by the output from the control device 7, and the amount of the refrigerant passing through the electronic control valve 11 is adjusted so that the blown air temperature becomes the set temperature.

(発明が解決しようとする問題点) 上記従来の冷凍装置においては、その冷凍能力制御運
転時にも電子式膨張弁3は蒸発器4がその最大冷凍能力
を発揮するように電子式膨張弁3を通る冷媒流量を調整
しており、この電子式膨張弁3を出た冷媒に電子式調整
弁11を流過した高温・高圧の冷媒ガスを合流させること
によって冷凍能力を減少させているため圧縮機1を通る
冷媒循環量は殆ど減少せず、従って、冷凍能力が小さい
にも拘らず圧縮機1の消費動力が殆ど変わらないという
問題があった。また、冷凍能力制御運転のためのバイパ
ス回路10及び電子式調整弁11を要するため、冷媒回路が
複雑になるのみならずこのためのコスト及び据付スペー
スが嵩むという問題があった。
(Problems to be Solved by the Invention) In the conventional refrigeration system described above, the electronic expansion valve 3 is provided so that the evaporator 4 exhibits its maximum refrigeration capacity even during the refrigeration capacity control operation. The refrigerant flow rate is adjusted, and the refrigerating capacity is reduced by combining the high-temperature and high-pressure refrigerant gas that has passed through the electronic control valve 11 with the refrigerant that has flowed out of the electronic expansion valve 3, thus reducing the compressor capacity. There is a problem in that the amount of refrigerant circulating through 1 hardly decreases, and therefore, the power consumption of the compressor 1 hardly changes despite the small refrigerating capacity. Further, since the bypass circuit 10 and the electronic control valve 11 for the refrigerating capacity control operation are required, there is a problem that the refrigerant circuit becomes complicated and the cost and installation space for this are increased.

(問題点を解決するための手段) 本発明は上記問題点に対処するために発明されたもの
であって、その要旨とするところは、圧縮機、凝縮器、
電子式膨張弁及び蒸発器をこの順に冷媒が循環する冷凍
装置において、前記蒸発器の出口の冷媒温度及び圧力並
びに被冷却媒体の温度を検出する検出器を設けるととも
に、被冷却媒体温度が所定の上限温度TH以上のときは前
記蒸発器の出口冷媒温度及び圧力に基づいて算出された
冷媒過熱度が所定の冷媒過熱度になるよう前記電子式膨
張弁の開度を最大とし、被冷却媒体温度が所定の下限温
度TL以下のときは前記圧縮機を停止し、被冷却媒体温度
が前記上限温度THと下限温度TLとの間にあるときは前記
電子式膨張弁の開度を前記最大開度より小さく、かつ、
被冷却媒体温度と設定温度TSとの温度差に対応する開度
に制御する制御装置を設けたことを特徴とする冷凍装置
にある。
(Means for Solving Problems) The present invention was invented to address the above problems, and the gist of the present invention is to provide a compressor, a condenser,
In the refrigeration system in which the refrigerant circulates through the electronic expansion valve and the evaporator in this order, a detector for detecting the refrigerant temperature and pressure at the outlet of the evaporator and the temperature of the medium to be cooled is provided, and the temperature of the medium to be cooled is predetermined. When the upper limit temperature T H or higher, the opening degree of the electronic expansion valve is maximized so that the refrigerant superheat degree calculated based on the outlet refrigerant temperature and pressure of the evaporator becomes a predetermined refrigerant superheat degree, and the medium to be cooled is cooled. When the temperature is equal to or lower than the predetermined lower limit temperature T L, the compressor is stopped, and when the temperature of the medium to be cooled is between the upper limit temperature T H and the lower limit temperature T L , the opening degree of the electronic expansion valve is changed. Smaller than the maximum opening, and
A refrigeration apparatus is provided with a control device for controlling an opening degree corresponding to a temperature difference between a temperature of a medium to be cooled and a set temperature T S.

(作用) 本発明は上記構成を具えているため、被冷却媒体温度
が所定の上限温度TH以上のときは蒸発器の出口冷媒温度
及び圧力に基づいて算出された冷媒過熱度が所定の冷媒
過熱度になるよう電子式膨張弁の開度を最大とし、被冷
却媒体温度が所定の下限温度TL以下のときは圧縮機を停
止し、被冷却媒体温度が上限温度THと下限温度TLとの間
にあるときは電子式膨張弁の開度を上記最大開度より小
さく、かつ、被冷却媒体温度と設定温度TSとの温度差に
対応する開度に制御する。
(Operation) Since the present invention has the above configuration, when the temperature of the medium to be cooled is equal to or higher than the predetermined upper limit temperature T H, the refrigerant superheat degree calculated based on the outlet refrigerant temperature and pressure of the evaporator is the predetermined refrigerant. The degree of opening of the electronic expansion valve is maximized so that the superheat degree is reached, the compressor is stopped when the temperature of the medium to be cooled is equal to or lower than the predetermined lower limit temperature T L, and the temperature of the medium to be cooled is set to the upper limit temperature T H and the lower limit temperature T L. When it is between L and L , the degree of opening of the electronic expansion valve is controlled to be smaller than the above-mentioned maximum degree of opening and corresponding to the temperature difference between the temperature of the medium to be cooled and the set temperature T S.

(実施例) 本発明の1実施例を第1図ないし第5図を参照しなが
ら具体的に説明する。
(Embodiment) An embodiment of the present invention will be specifically described with reference to FIGS.

第1図には冷媒回路図が示され、1は圧縮機、2は凝
縮器、3は電子式膨張弁、4は蒸発器、5は冷媒温度検
出器、6は冷媒圧力検出器、8は吹出空気温度検出器、
9は温度設定器で、以上は第6図に示す従来のものと同
様である。
FIG. 1 is a refrigerant circuit diagram, in which 1 is a compressor, 2 is a condenser, 3 is an electronic expansion valve, 4 is an evaporator, 5 is a refrigerant temperature detector, 6 is a refrigerant pressure detector, and 8 is a refrigerant pressure detector. Blown air temperature detector,
Reference numeral 9 is a temperature setting device, and the above is the same as the conventional one shown in FIG.

蒸発器4に吸込まれる空気温度を検出するための吸込
空気温度検出器12が設けられる。そして、制御装置21に
は冷媒温度検出器5、冷媒圧力検出器6、吹出空気温度
検出器8、吸込空気温度検出器12及び温度設定器9から
の信号が入力され、この制御装置21からの出力によって
電子式膨張弁3及び圧縮機1が制御される。
An intake air temperature detector 12 for detecting the temperature of the air sucked into the evaporator 4 is provided. Then, signals from the refrigerant temperature detector 5, the refrigerant pressure detector 6, the blown air temperature detector 8, the intake air temperature detector 12 and the temperature setting device 9 are input to the control device 21, and the control device 21 outputs signals. The output controls the electronic expansion valve 3 and the compressor 1.

制御装置21の機能ブロック図が第2図に示され、その
フローチャートが第3図に示されている。
A functional block diagram of the control device 21 is shown in FIG. 2, and its flowchart is shown in FIG.

第3図において、ステップで吹出空気温度検出器8
からの吹出空気温度又は吸込空気温度検出器12からの吸
込空気温度が制御装置21の温度差算出回路211に入力さ
れ、ステップで温度設定器9からの設定温度が温度差
算出回路211に入力される。次いで、ステップで温度
差算出回路211により吹出空気温度又は吸込空気温度と
設定温度との間の温度差が算出される。しかる後、ステ
ップで、冷凍能力が適当か否かが判断され、適当と判
断された場合にはステップに戻るが、過大と判断され
た場合には、ステップで弁開度出力指令回路212を経
て電子式膨張弁3にその開度を小にする旨の出力信号が
出力される。過小と判断された場合にはステップで弁
開度出力指令回路212を経て電子式膨張弁3にその開度
を大にする旨の出力信号が出力される。しかして、第4
図に示すように膨張弁開度Aで最大の冷凍能力Q1を発揮
し、これ以下の膨張弁開度例えばBでは、冷凍能力Q2
低下する。なお、膨張弁開度がA以上になると冷媒の一
部が液のまま圧縮機1に戻り、圧縮機1が破損するので
膨張弁開度がA以上に大きくなることはない。
In FIG. 3, the blown air temperature detector 8 is stepwise.
From the intake air temperature detector 12 or the intake air temperature from the intake air temperature detector 12 is input to the temperature difference calculation circuit 211 of the control device 21, and the set temperature from the temperature setter 9 is input to the temperature difference calculation circuit 211 in step. It Next, at step, the temperature difference calculation circuit 211 calculates the temperature difference between the blown air temperature or the intake air temperature and the set temperature. Then, in step, it is determined whether or not the refrigerating capacity is appropriate, and if it is determined to be appropriate, the process returns to step, but if it is determined to be excessive, in step the valve opening output command circuit 212 is passed. An output signal for reducing the opening is output to the electronic expansion valve 3. If it is judged to be too small, an output signal for increasing the opening is output to the electronic expansion valve 3 through the valve opening output command circuit 212 in step. Then, the fourth
As shown in the figure, the maximum refrigerating capacity Q 1 is exhibited at the expansion valve opening A, and the refrigerating capacity Q 2 is reduced at an expansion valve opening less than this, for example, B. When the expansion valve opening becomes A or more, a part of the refrigerant returns to the compressor 1 as a liquid and the compressor 1 is damaged, so that the expansion valve opening does not become larger than A.

しかして、第5図に示すように、吹出空気温度又は吸
込空気温度が温度TH以上の場合には最大能力運転が行わ
れ、制御装置21は冷媒温度検出器5で検出された蒸発器
4の出口の冷媒温度が冷媒圧力検出器6で検出された蒸
発器4の出口の冷媒圧力に対応する飽和温度より約5deg
位過熱されるように電子式膨張弁3の開度を制御する。
吹出空気温度又は吸込空気温度が温度TL以下の場合には
制御装置21は圧縮機1に出力してこれを停止させる。そ
して、温度THとTLの間、即ち、設定温度Tsの上下数度の
範囲内で冷凍能力制御運転が行われ、吹出空気温度又は
吸込空気温度は次第に設定温度Tsに収束する。
Then, as shown in FIG. 5, when the blown air temperature or the sucked air temperature is equal to or higher than the temperature T H , the maximum capacity operation is performed, and the control device 21 controls the evaporator 4 detected by the refrigerant temperature detector 5. The refrigerant temperature at the outlet of the refrigerant is about 5 degrees below the saturation temperature corresponding to the refrigerant pressure at the outlet of the evaporator 4 detected by the refrigerant pressure detector 6.
The opening of the electronic expansion valve 3 is controlled so that it is overheated.
When the blown air temperature or the sucked air temperature is equal to or lower than the temperature T L , the control device 21 outputs it to the compressor 1 and stops it. Then, the refrigerating capacity control operation is performed between the temperatures T H and T L , that is, within a range of several degrees above and below the set temperature T s , and the outlet air temperature or the intake air temperature gradually converges to the set temperature T s .

この結果、冷凍能力制御運転中、電子式膨張弁3の開
度は冷凍負荷に見合うように最大能力時より小さくさ
れ、従って、電子式膨張弁3を通って循環する冷媒量が
減少するので、圧縮機1の消費動力も低減する。以上、
本発明を空気調和機に適用した例について説明したが、
蒸発器4によって冷却される被冷却媒体は液体又は固体
であっても良い。
As a result, during the refrigerating capacity control operation, the opening degree of the electronic expansion valve 3 is made smaller than that at the maximum capacity so as to correspond to the refrigerating load, and therefore, the amount of refrigerant circulating through the electronic expansion valve 3 is reduced. The power consumption of the compressor 1 is also reduced. that's all,
Although the example in which the present invention is applied to an air conditioner has been described,
The cooled medium cooled by the evaporator 4 may be liquid or solid.

(発明の効果) 本発明においては、被冷却媒体温度が所定の上限温度
TH以上のときは、蒸発器の出口冷媒温度及び圧力に基づ
いて算出された冷媒過熱度が所定の冷媒過熱度になるよ
う電子式膨張弁の開度を最大とすることによって最大の
冷凍能力を発揮させることができるので、被冷却媒体温
度を早急に設定温度Tsに近付けることができる。
(Effect of the Invention) In the present invention, the temperature of the medium to be cooled is the predetermined upper limit temperature.
When T H or higher, the maximum refrigerating capacity is achieved by maximizing the opening degree of the electronic expansion valve so that the refrigerant superheat degree calculated based on the evaporator outlet refrigerant temperature and pressure becomes the predetermined refrigerant superheat degree. Therefore, the temperature of the medium to be cooled can be quickly brought close to the set temperature T s .

そして、電子式膨張弁の開度は最大の開度以上になら
ないため液冷媒が圧縮機に戻ることによる圧縮機の破損
を防止できる。
Further, since the opening degree of the electronic expansion valve does not exceed the maximum opening degree, it is possible to prevent the compressor from being damaged due to the liquid refrigerant returning to the compressor.

また、被冷却媒体温度が所定の下限温度TL以下のとき
は、圧縮機が停止するので、圧縮機の消費動力を節減で
きる。
Further, when the temperature of the medium to be cooled is equal to or lower than the predetermined lower limit temperature T L , the compressor is stopped, so that the power consumption of the compressor can be saved.

更に、被冷却媒体温度が上限温度THと下限温度TLとの
間にあるときは、電子式膨張弁の開度を最大開度より小
さく、かつ、被冷却媒体温度と設定温度Tsとの温度差に
対応する開度に制御することによって冷凍能力を最大能
力より低減できる。
Further, when the cooled medium temperature is between the upper limit temperature T H and the lower limit temperature T L , the opening degree of the electronic expansion valve is smaller than the maximum opening degree, and the cooled medium temperature and the set temperature T s The refrigerating capacity can be reduced from the maximum capacity by controlling the opening degree corresponding to the temperature difference of.

従って、冷凍能力制御運転時における冷媒循環量は最
大能力運転時のそれより減少するので、圧縮機の消費動
力も低減する。
Therefore, since the refrigerant circulation amount during the refrigerating capacity control operation is smaller than that during the maximum capacity operation, the power consumption of the compressor is also reduced.

また、従来のバイパス回路及びこれを開閉する電子式
調整弁を省くことができるので、冷媒回路が簡素化され
るのみならずコスト及び据付スペースを節減できる。
Further, since the conventional bypass circuit and the electronic adjusting valve for opening and closing the bypass circuit can be omitted, not only the refrigerant circuit can be simplified, but also the cost and the installation space can be saved.

【図面の簡単な説明】[Brief description of drawings]

第1図ないし第5図は本発明の1実施例を示し、第1図
は冷媒回路図、第2図は制御装置の機能ブロック図、第
3図は制御装置のフローチャート、第4図は膨張弁開度
と冷凍能力との関係を示す線図、第5図は被冷却媒体温
度と運転態様との関係を示す線図でる。第6図は従来の
冷凍装置の冷媒回路図である。 圧縮機……1、凝縮器……2、電子式膨張弁……3、蒸
発器……4、制御装置……21、冷媒温度検出器……5、
冷媒圧力検出器……6、被冷却媒体温度検出器……8、
12、温度設定器……9
1 to 5 show one embodiment of the present invention, FIG. 1 is a refrigerant circuit diagram, FIG. 2 is a functional block diagram of a control device, FIG. 3 is a flow chart of the control device, and FIG. FIG. 5 is a diagram showing the relationship between the valve opening and the refrigerating capacity, and FIG. 5 is a diagram showing the relationship between the temperature of the medium to be cooled and the operating mode. FIG. 6 is a refrigerant circuit diagram of a conventional refrigeration system. Compressor …… 1, condenser …… 2, electronic expansion valve …… 3, evaporator …… 4, control unit …… 21, refrigerant temperature detector …… 5,
Refrigerant pressure detector …… 6, Cooled medium temperature detector …… 8,
12, temperature setting device ... 9

───────────────────────────────────────────────────── フロントページの続き (72)発明者 山下 敏雄 愛知県西春日井郡西枇杷島町字旭町3丁目 1番地 三菱重工業株式会社名古屋冷熱工 場内 (72)発明者 不殿 寛爾 愛知県名古屋市中村区岩塚町字高道1番地 三菱重工業株式会社名古屋研究所内 (56)参考文献 特開 昭60−196569(JP,A) 特開 昭60−185075(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Toshio Yamashita Toshio Yamashita 3-1, Asahi-cho, Nishibiwajima-cho, Nishi-Kasugai-gun, Aichi Prefecture Mitsubishi Heavy Industries, Ltd. Nagoya Cold Energy Plant (72) Inventor Kan, Nakamura, Naka City, Aichi Prefecture No. 1 Takamichi, Iwatsuka-cho, Ward, Nagoya Research Institute, Mitsubishi Heavy Industries, Ltd. (56) Reference JP-A-60-196569 (JP, A) JP-A-60-185075 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】圧縮機、凝縮器、電子式膨張弁及び蒸発器
をこの順に冷媒が循環する冷凍装置において、前記蒸発
器の出口の冷媒温度及び圧力並びに被冷却媒体の温度を
検出する検出器を設けるとともに、被冷却媒体温度が所
定の上限温度TH以上のときは前記蒸発器の出口冷媒温度
及び圧力に基づいて算出された冷媒過熱度が所定の冷媒
過熱度になるよう前記電子式膨張弁の開度を最大とし、
被冷却媒体温度が所定の下限温度TL以下のときは前記圧
縮機を停止し、被冷却媒体温度が前記上限温度THと下限
温度TLとの間にあるときは前記電子式膨張弁の開度を前
記最大開度より小さく、かつ、被冷却媒体温度と設定温
度TSとの温度差に対応する開度に制御する制御装置を設
けたことを特徴とする冷凍装置。
1. A refrigeration system in which a refrigerant circulates through a compressor, a condenser, an electronic expansion valve and an evaporator in this order, and a detector for detecting the refrigerant temperature and pressure at the outlet of the evaporator and the temperature of a medium to be cooled. When the temperature of the medium to be cooled is equal to or higher than a predetermined upper limit temperature T H, the electronic expansion is performed so that the refrigerant superheat degree calculated based on the outlet refrigerant temperature and pressure of the evaporator becomes the predetermined refrigerant superheat degree. Maximum valve opening,
When the cooled medium temperature is equal to or lower than a predetermined lower limit temperature T L, the compressor is stopped, and when the cooled medium temperature is between the upper limit temperature T H and the lower limit temperature T L , the electronic expansion valve A refrigeration system provided with a control device for controlling the opening to be smaller than the maximum opening and controlling the opening to correspond to the temperature difference between the temperature of the medium to be cooled and the set temperature T S.
JP62090514A 1987-04-13 1987-04-13 Refrigeration equipment Expired - Lifetime JPH0833242B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62090514A JPH0833242B2 (en) 1987-04-13 1987-04-13 Refrigeration equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62090514A JPH0833242B2 (en) 1987-04-13 1987-04-13 Refrigeration equipment

Publications (2)

Publication Number Publication Date
JPS63259353A JPS63259353A (en) 1988-10-26
JPH0833242B2 true JPH0833242B2 (en) 1996-03-29

Family

ID=14000570

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62090514A Expired - Lifetime JPH0833242B2 (en) 1987-04-13 1987-04-13 Refrigeration equipment

Country Status (1)

Country Link
JP (1) JPH0833242B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017109905A1 (en) * 2015-12-24 2017-06-29 三菱電機株式会社 Air-conditioning/hot-water supplying combined system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2503636B2 (en) * 1989-03-20 1996-06-05 ダイキン工業株式会社 Refrigeration system operation controller
JP5106819B2 (en) * 2006-10-20 2012-12-26 三菱重工業株式会社 HEAT SOURCE DEVICE, HEAT SOURCE SYSTEM, AND HEAT SOURCE DEVICE CONTROL METHOD

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60185075A (en) * 1984-03-02 1985-09-20 株式会社日立製作所 Refrigerant flow control device
JPS60196569A (en) * 1984-03-19 1985-10-05 三洋電機株式会社 Controller for flow rate of refrigerant

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017109905A1 (en) * 2015-12-24 2017-06-29 三菱電機株式会社 Air-conditioning/hot-water supplying combined system

Also Published As

Publication number Publication date
JPS63259353A (en) 1988-10-26

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