JPH0772648B2 - Refrigerant flow control method - Google Patents
Refrigerant flow control methodInfo
- Publication number
- JPH0772648B2 JPH0772648B2 JP59208284A JP20828484A JPH0772648B2 JP H0772648 B2 JPH0772648 B2 JP H0772648B2 JP 59208284 A JP59208284 A JP 59208284A JP 20828484 A JP20828484 A JP 20828484A JP H0772648 B2 JPH0772648 B2 JP H0772648B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- expansion valve
- compressor
- temperature
- operation mode
- 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 - Fee Related
Links
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (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、冷凍サイクルにおける冷媒流量制御装置に係
り、特に冷凍空調装置全般に用いられるパルスモータ駆
動式膨張弁の絞り量を、あらかじめ設定した制御手順に
従って制御するのに好適な、冷凍サイクルにおける冷媒
流量制御装置に関するものである。Description: TECHNICAL FIELD The present invention relates to a refrigerant flow rate control device in a refrigeration cycle, and in particular, presets a throttle amount of a pulse motor driven expansion valve used in all refrigeration air conditioners. The present invention relates to a refrigerant flow rate control device in a refrigeration cycle, which is suitable for controlling according to a control procedure.
圧縮機,凝縮器,膨張手段,蒸発器を冷媒流路で接続し
て冷凍サイクルを構成している冷凍空調装置において、
前記膨張手段として、電気信号によって絞り量が調節可
能な電動式膨張弁を用いているものでは、蒸発器出口部
あるいは圧縮機入口部の冷媒温度すなわち冷媒過熱度を
サーミスタなどの温度センサで検出して、その過熱度が
一定となるように電動式膨張弁の絞り量を調節してい
る。In a refrigerating and air-conditioning apparatus that constitutes a refrigeration cycle by connecting a compressor, a condenser, an expansion means, and an evaporator with a refrigerant flow path,
In the case of using an electric expansion valve whose throttle amount can be adjusted by an electric signal as the expansion means, the refrigerant temperature at the evaporator outlet or the compressor inlet, that is, the refrigerant superheat is detected by a temperature sensor such as a thermistor. The throttle amount of the electric expansion valve is adjusted so that the degree of superheat is constant.
このような冷凍装置の制御の例が特開昭55−116068号公
報、特開昭55−152360号公報に記載されている。また、
過渡状態に対する膨張弁制御の他の方法が、特開昭56−
44566号公報に開示されている。この従来例では、凝縮
器入口部ないし中間部にも温度センサを設け、凝縮温度
を検出して、圧縮機の始動から凝縮温度が所定値に達す
るまでは膨張弁開度を全開にし、その後過熱度制御を行
っている。Examples of control of such a refrigerating apparatus are described in JP-A-55-116068 and JP-A-55-152360. Also,
Another method of controlling an expansion valve for a transient state is disclosed in Japanese Patent Laid-Open No. 56-
It is disclosed in Japanese Patent No. 44566. In this conventional example, a temperature sensor is also provided at the inlet or intermediate part of the condenser to detect the condensing temperature, and the expansion valve opening is fully opened from the start of the compressor until the condensing temperature reaches a predetermined value, and then overheating is performed. Degree control.
上記従来の装置においては、定常運転時には良好な制御
が行えるが、圧縮機始動時などの急速な過渡状態に対し
ては、温度センサの検知遅れなどにより電動式膨張弁の
制御が冷凍サイクルの変化に追従できず、蒸発器出口部
あるいは圧縮機入口部の冷媒過熱度が過大となり、冷凍
サイクルの立上り時間が長くなっていた。また、上記特
開昭55−116068号公報、特開昭55−152360号公報に記載
のものにおいては、蒸発器の負荷が大きく変動すること
について考慮されているものの、必ずしも満足のいく時
間内で好ましい運転状態にすることができなかった。In the above conventional device, good control can be performed during steady operation, but for rapid transient conditions such as when the compressor starts, the control of the electric expansion valve changes the refrigeration cycle due to the detection delay of the temperature sensor. However, the refrigerant superheat at the evaporator outlet or the compressor inlet was too large, and the rise time of the refrigeration cycle was long. Further, in the above-mentioned JP-A-55-116068 and JP-A-55-152360, although it is taken into consideration that the load of the evaporator fluctuates significantly, it is not always within a satisfactory time. It was not possible to achieve the desired operating conditions.
さらに、上記特開昭56−44566号公報に記載のものは圧
縮機始動時の過渡状態から定常状態への移行が円滑に行
われるという優れた効果を奏するものであるが、制御段
階の切換えのタイミングに凝縮温度を用いているため蒸
発器出口部では過熱度が過大となり、液戻り状態となる
不具合が生じる恐れがある。Further, the one described in JP-A-56-44566 has an excellent effect that the transition from the transient state at the time of starting the compressor to the steady state is smoothly performed, but it is possible to change the control stage. Since the condensing temperature is used for the timing, the degree of superheat at the evaporator outlet may be excessive, which may cause a liquid return condition.
また、一般に、膨張弁の最大開度と定常状態での最適開
度が大きく異なる場合には、定常制御に切換えた後設定
した過熱度になるまでに多くの時間を要するという不具
合があった。Further, in general, when the maximum opening degree of the expansion valve and the optimum opening degree in the steady state are significantly different, there is a problem that it takes a lot of time until the set superheat degree is reached after switching to the steady control.
本発明は上記従来の技術の課題を解決するためになされ
たもので、制御性の良いパルスモータ駆動式の膨張弁を
用いたときに、センサの応答性が不十分な事に起因する
圧縮機の始動直後の冷凍サイクルの立上り特性の不具合
を改善することを目的とする。具体的には圧縮機の始動
直後に蒸発器に流入する冷媒量を多くし、蒸発器の機能
を有効に活用して立上り特性の良好な冷媒流量制御方法
を実現することにある。The present invention has been made to solve the above-mentioned problems of the conventional technology, and when a pulse motor drive type expansion valve with good controllability is used, the compressor is caused by insufficient response of the sensor. The purpose is to improve the problems of the start-up characteristics of the refrigeration cycle immediately after the start of the. Specifically, the amount of refrigerant flowing into the evaporator is increased immediately after the compressor is started, and the function of the evaporator is effectively utilized to realize a refrigerant flow rate control method having a good start-up characteristic.
上記目的を達成するために、圧縮機と、凝縮器と、電気
信号によって絞り量が調節可能なパルスモータ駆動式の
膨張弁と、蒸発器とを冷媒配管で順次接続して形成され
た冷凍サイクル内を流通する冷媒量を制御する冷媒流量
制御方法であって、前記圧縮機の始動後の過渡運転モー
ドと、この過渡運転モード経過後の定常運転モードとを
有し、前記過渡運転モードは前記圧縮機の始動後の所定
時間(τs1)は前記膨張弁の絞り量を最小とし、その後
予め設定した時間中、第1の温度センサにより検出され
た前記蒸発器の冷媒蒸発温度(Te)と第2の温度センサ
により検出された前記蒸発器出口部あるいは前記圧縮機
入口部の冷媒温度(Ts)との検出温度差を求め、前記検
出温度差が設定温度差(SHa)に近づくよう前記膨張弁
の絞り量を所定時間(τs2)間隔毎に段階的にかつ予め
設定された所定の絞り量まで単調増加させて前記蒸発器
の過熱度を徐々に増加させるとともに、前記予め設定し
た時間が経過したときに前記過渡運転モードから定常運
転モードに移行するものである。To achieve the above object, a refrigeration cycle formed by sequentially connecting a compressor, a condenser, a pulse motor drive type expansion valve whose throttle amount can be adjusted by an electric signal, and an evaporator with a refrigerant pipe. A method of controlling a refrigerant flow rate for controlling the amount of refrigerant flowing through, having a transient operation mode after the start of the compressor and a steady operation mode after this transient operation mode has elapsed, wherein the transient operation mode is the A predetermined amount of time (τ s1 ) after the start of the compressor minimizes the expansion amount of the expansion valve, and thereafter, during a preset time, the refrigerant evaporation temperature (Te) of the evaporator detected by the first temperature sensor The detected temperature difference with the refrigerant temperature (Ts) at the evaporator outlet or the compressor inlet detected by the second temperature sensor is obtained, and the expansion is performed so that the detected temperature difference approaches the set temperature difference (SHa). Adjust the valve throttle amount for a predetermined time ( τ s2 ) The superheat degree of the evaporator is gradually increased by monotonically increasing to a predetermined preset throttle amount every interval, and the transient operation mode is set when the preset time elapses. From the normal operation mode.
なお、付記すると本発明は、定常運転時は蒸発器出口部
あるいは圧縮機入口部の冷媒過熱度が一定となるように
膨張弁の絞り量を制御するものである。It should be noted that the present invention controls the expansion amount of the expansion valve so that the refrigerant superheat degree at the evaporator outlet portion or the compressor inlet portion becomes constant during steady operation.
本発明においては、膨張弁にパルスモータ駆動式の膨張
弁を用いたときに、センサの応答性の不十分さに起因す
る圧縮機始動時の冷凍サイクルの不安定性を解消するた
めに、圧縮機の始動とともに膨張弁の絞り量を最小と
し、膨張弁を流れる冷媒量を多くすることにより、始動
直後の蒸発温度Teの低下割合が小さく、また吸入冷媒温
度Tsとの温度差(Ts−Te)を小さくしている。これによ
り、始動から定常に達するまでの時間が短くなり、立上
り時間が著しく短縮される。In the present invention, when a pulse motor drive type expansion valve is used as the expansion valve, in order to eliminate the instability of the refrigeration cycle at the time of starting the compressor due to insufficient response of the sensor, the compressor is By increasing the amount of refrigerant flowing through the expansion valve and minimizing the amount of expansion of the expansion valve as the engine starts, the rate of decrease in the evaporation temperature Te immediately after startup is small, and the temperature difference from the intake refrigerant temperature Ts (Ts-Te) Is small. As a result, the time from the start to the steady state is shortened, and the rise time is significantly shortened.
また、膨張弁の絞り量最小の状態から定常運転の制御に
切換えるまでの間に、絞り量を温度差(Ts−Te)に応じ
て段階的に調節しているために定常運転の制御への切換
えが円滑に行われる。つまり、膨張弁開度のみを合わせ
ようとして早期に膨張弁を絞ると過熱度は目標過熱度を
越えて変化し、さらに目標過熱度に近付けるために膨張
弁を開くと言うような工程を繰り返すのに対し、本発明
では段階的に絞り量を変えているので、漸近的に目標過
熱度に達する。さらに、絞りを一様に変化させる場合に
は、開度目標に対して常に実際の開度が遅れるため、漸
近的ではあるがゆっくりとした変化であり、本発明では
段階的であるから所定時間(τs2)ごとに過熱度の目標
値へ達する時間を早めることができる。In addition, since the expansion amount is adjusted stepwise according to the temperature difference (Ts-Te) from the state where the expansion valve is at the minimum throttle amount to the control for steady operation, the steady operation control Switching is smoothly performed. That is, if the expansion valve is throttled early in an attempt to match only the opening degree of the expansion valve, the degree of superheat changes beyond the target degree of superheat, and the process of opening the expansion valve to bring it closer to the target degree of superheat is repeated. On the other hand, in the present invention, since the throttle amount is changed stepwise, the target superheat degree is asymptotically reached. Further, when the aperture is changed uniformly, the actual opening is always delayed with respect to the opening target, so that the change is asymptotic but slow, and in the present invention, it is a stepwise change, so Each (τ s2 ) can shorten the time to reach the target value of superheat.
以下、本発明の各実施例を第1図ないし第4図を参照し
て説明する。まず、第1図は、本発明の一実施例に係る
冷凍サイクルにおける冷媒流量制御装置の構成図、第2
図は、第1図の装置の電動式膨張弁の制御フローチャー
トで、(a)圧縮機始動時、(b)は定常運転時のフロ
ーを示している。Embodiments of the present invention will be described below with reference to FIGS. 1 to 4. First, FIG. 1 is a configuration diagram of a refrigerant flow rate control device in a refrigeration cycle according to an embodiment of the present invention, and FIG.
The figure is a control flowchart of the electric expansion valve of the apparatus of FIG. 1, and (a) shows the flow at the time of starting the compressor, and (b) shows the flow at the time of steady operation.
第1図において、1は圧縮機、2は凝縮器、3は電気信
号によって絞り量が調節可能な電動式膨張弁、4は蒸発
器で、これら機器を冷媒流路で接続して冷凍サイクルが
構成されている。In FIG. 1, 1 is a compressor, 2 is a condenser, 3 is an electric expansion valve whose throttle amount can be adjusted by an electric signal, and 4 is an evaporator. It is configured.
5は蒸発器の冷媒蒸発温度を検出するサーミスタなど第
1の温度センサ、6は蒸発器出口部あるいは圧縮機入口
部の冷媒温度すなわち冷媒過熱度を検出するサーミスタ
など第2の温度センサ、7は電動式膨張弁3の冷媒絞り
量を制御するための制御装置に係り、たとえばマイコン
などのように情報の入力、記憶、比較判断、計算、電気
信号の出力発信等を行う演算制御装置である。5 is a first temperature sensor such as a thermistor for detecting the refrigerant evaporation temperature of the evaporator, 6 is a second temperature sensor such as a thermistor for detecting the refrigerant temperature at the evaporator outlet or the compressor inlet, that is, the degree of refrigerant superheat, 7 is The arithmetic control device is related to a control device for controlling the refrigerant throttle amount of the electrically driven expansion valve 3, and is, for example, a microcomputer that performs information input, storage, comparison / judgment, calculation, electric signal output transmission, and the like.
前記冷凍サイクルにおける冷媒の流れは、圧縮機1→凝
縮器2→電動式膨張弁3→蒸発器4→圧縮機1の順に循
環する。The flow of the refrigerant in the refrigeration cycle circulates in the order of compressor 1 → condenser 2 → motorized expansion valve 3 → evaporator 4 → compressor 1.
たとえば、このような冷凍サイクルの冷凍空調装置で
は、圧縮機1から吐出される高温高圧の冷媒ガスは凝縮
器において外部空気などと熱交換し放熱して冷媒みずか
らは凝縮する。凝縮液化した冷媒は電動式膨張弁3を経
て膨張減圧され蒸発器4に入る。ここで冷媒は室内空気
などから気化熱を奪って冷房効果をあげ、冷媒みずから
は蒸発し低温低圧の冷媒ガスとなって圧縮機1に戻り、
以下同じサイクルを繰返す。For example, in such a refrigeration air-conditioning apparatus of a refrigeration cycle, the high-temperature and high-pressure refrigerant gas discharged from the compressor 1 exchanges heat with external air and the like in the condenser and radiates heat to condense from the refrigerant itself. The condensed and liquefied refrigerant is expanded and decompressed through the electric expansion valve 3 and enters the evaporator 4. Here, the refrigerant removes heat of vaporization from room air or the like to enhance the cooling effect, evaporates from the refrigerant itself and becomes low-temperature low-pressure refrigerant gas, and returns to the compressor 1.
The same cycle is repeated thereafter.
次に電動式膨張弁3の冷媒流量制御について説明する。Next, the refrigerant flow rate control of the electric expansion valve 3 will be described.
まず、第2図(b)に示す定常運転時の制御手順につい
て説明する。First, the control procedure during steady operation shown in FIG. 2 (b) will be described.
第1図に示される演算制御装置7は、あらかじめ設定さ
れた時間間隔τaで、蒸発温度Teと、圧縮機入口部の吸
入冷媒温度(過熱度)Tsを、第1,第2の温度センサ5,6
により検出する。検出された温度差(Ts−Te)が、あら
かじめ設定された温度差の値SHaより小さい場合には、
演算制御装置7は、その旨の電気信号を発して電動式膨
張弁3の絞り量を大きくする。絞り量を大きくすれば冷
媒流量が減り(Ts−Te)が増加する。The arithmetic and control unit 7 shown in FIG. 1 detects the evaporation temperature Te and the suction refrigerant temperature (superheat degree) Ts at the inlet of the compressor at a preset time interval τa by using the first and second temperature sensors 5 , 6
To detect. When the detected temperature difference (Ts-Te) is smaller than the preset temperature difference value SHa,
The arithmetic and control unit 7 emits an electric signal to that effect to increase the throttle amount of the electric expansion valve 3. If the throttle amount is increased, the flow rate of the refrigerant decreases and Ts-Te increases.
また逆に、検出された温度差(Ts−Te)が、あらかじめ
設定された温度差の値SHaより大きい場合は、その旨の
電気信号を発して電動式膨張弁3の絞り量を小さくす
る。絞り量を小さくすれば冷媒流量が増え(Ts−Te)が
低下する。Conversely, when the detected temperature difference (Ts-Te) is larger than the preset temperature difference value SHa, an electric signal to that effect is issued to reduce the throttle amount of the electrically driven expansion valve 3. If the throttle amount is reduced, the refrigerant flow rate increases (Ts-Te).
このように検出された温度差(Ts−Te)が設定された温
度差の値、すなわち設定温度SHaとなるように電動式膨
張弁3の絞り量が調節される。The throttle amount of the electrically driven expansion valve 3 is adjusted so that the temperature difference (Ts-Te) thus detected becomes the set temperature difference value, that is, the set temperature SHa.
次に、第2図(a)に示す圧縮機始動時の制御手順を説
明する。Next, a control procedure at the time of starting the compressor shown in FIG. 2 (a) will be described.
演算制御装置7には、あらかじめ設定した次に述べる制
御手順が入力されており、その制御手順に従って電動式
膨張弁3の絞り量を調節する電気信号を出力する。A preset control procedure described below is input to the arithmetic and control unit 7, and an electric signal for adjusting the throttle amount of the electric expansion valve 3 is output according to the control procedure.
圧縮機1の始動とともに電動式膨張弁3の絞り量を最小
とし、あらかじめ設定された一定時間τs1の間その状態
を保つ。When the compressor 1 is started, the throttle amount of the electric expansion valve 3 is minimized and the state is maintained for a preset constant time τs 1 .
τs1経過後は、あらかじめ設定された時間間隔τs2で、
蒸発温度Teと、圧縮機入口部の吸入冷媒温度Tsを温度セ
ンサ5,6により検出し、検出された温度差(Ts−Te)が
設定温度SHaより小さい場合には、電動式膨張弁3の絞
り量を大きくする。時間間隔τs2ごとに、この動作を行
うことにより段階的に電動式膨張弁3の絞り量は増加す
る。After τs 1 has elapsed, at a preset time interval τs 2 ,
The evaporation temperature Te and the suction refrigerant temperature Ts at the compressor inlet are detected by the temperature sensors 5 and 6, and when the detected temperature difference (Ts−Te) is smaller than the set temperature SHa, the electric expansion valve 3 Increase the aperture. By performing this operation at every time interval τ s 2 , the throttle amount of the electric expansion valve 3 is increased stepwise.
その絞り量があらかじめ設定された所定絞り量になった
場合には膨張弁開度を変えず、あらかじめ設定された時
間が経過すると、先に第2図(b)で説明した定常運転
時の制御に移行する。When the throttle amount reaches a preset predetermined throttle amount, the expansion valve opening is not changed, and when the preset time elapses, the control during the steady operation described above with reference to FIG. 2 (b). Move to.
以上説明した制御を行った場合の運転例を第3図に示
す。An example of operation when the above-described control is performed is shown in FIG.
第3図は、圧縮機の始動から定常運転までの膨張弁絞り
量,冷媒温度の変化を示す線図で、横軸に時間経過をと
り、縦軸に膨張弁絞り量と、冷媒温度すなわち冷媒蒸発
温度Te,圧縮機入口部の吸入冷媒温度Tsをとっている。
実線は、本発明の一実施例による運転例、破線は、上記
始動時の制御を行わない従来技術の運転例を示して対比
している。FIG. 3 is a diagram showing changes in the expansion valve throttle amount and the refrigerant temperature from the start of the compressor to the steady operation. The horizontal axis indicates time, the vertical axis indicates the expansion valve throttle amount, and the refrigerant temperature, that is, the refrigerant temperature. The evaporation temperature Te and the suction refrigerant temperature Ts at the compressor inlet are taken.
The solid line shows an operation example according to one embodiment of the present invention, and the broken line shows an operation example of the related art in which the control at the time of starting is not performed for comparison.
ここでは、電動式膨張弁としてパルスモータ駆動式膨張
弁を使用した例を示し、始動前の膨張弁絞り量は、圧縮
機停止前の絞り量である。図から明らかなように、本実
施例では、圧縮機の始動とともに膨張弁の絞り量を最小
とするために、膨張弁を流れる冷媒量が多くなり、始動
直後の蒸発温度Teの低下割合が小さく、また吸入冷媒温
度Tsとの温度差(Ts−Te)も小さくなっている。Here, an example in which a pulse motor driven expansion valve is used as the electric expansion valve is shown, and the expansion valve throttle amount before starting is the throttle amount before stopping the compressor. As is clear from the figure, in the present embodiment, in order to minimize the expansion amount of the expansion valve with the start of the compressor, the amount of refrigerant flowing through the expansion valve increases, and the decrease rate of the evaporation temperature Te immediately after the start is small. Also, the temperature difference (Ts-Te) from the suction refrigerant temperature Ts is small.
また、実線で示す本実施例の運転の方が、始動から定常
に達するまでの時間も短くなっており、本実施例により
立上り時間が著しく短縮されていることがわかる。Further, in the operation of this embodiment shown by the solid line, the time from the start to the steady state is shorter, and it can be seen that the rising time is significantly shortened by this embodiment.
また、膨張弁の絞り量最小の状態から定常運転の制御に
切換えるまでの間に、絞り量を温度差(Ts−Te)に応じ
て段階的に調節しているために定常運転の制御への切換
えが円滑に行われる。In addition, since the expansion amount is adjusted stepwise according to the temperature difference (Ts-Te) from the state where the expansion valve is at the minimum throttle amount to the control for steady operation, the steady operation control Switching is smoothly performed.
上述した実施例では、電動式膨張弁の絞り量が最小の時
点から定常運転の制御に移行するまでの間の絞り量の増
加を、圧縮機入口部の冷媒過熱度に応じて制御している
が、第4図に示すように、あらかじめ設定された制御パ
ターンで、装置の始動特性に応じた絞り量の時間的変化
で制御してもよい。In the above-described embodiment, the increase of the throttle amount from the time when the throttle amount of the electric expansion valve is minimum to the time of shifting to the control of the steady operation is controlled according to the degree of refrigerant superheat at the inlet of the compressor. However, as shown in FIG. 4, control may be performed by a preset control pattern by temporal change of the aperture amount according to the starting characteristics of the device.
第4図は、本発明の他の実施例に係る冷媒サイクルにお
ける冷媒流量制御装置の制御パターンを示す線図であ
り、横軸に時間経過,縦軸に膨張弁絞り量をとるもの
で、先の第3図に示した膨張弁絞り量の変化の図に対応
する線図である。FIG. 4 is a diagram showing a control pattern of a refrigerant flow rate control device in a refrigerant cycle according to another embodiment of the present invention, in which the abscissa axis indicates time passage and the ordinate axis indicates expansion valve throttle amount. FIG. 4 is a diagram corresponding to the diagram of changes in expansion valve throttle amount shown in FIG. 3.
このように、第4図の例では、圧縮機の始動とともに膨
張弁の絞り量を最小とし、その後、段階的に絞り量を増
加させる制御パターンを、蒸発器出口部あるいは圧縮機
入口部の冷媒過熱度に応じて制御するのではなく、その
装置の始動特性に応じた絞り量の時間的変化をあらかじ
め設定し、演算制御装置に記憶させておき、記憶させた
制御手順の制御パターンに従って運転するようにしたも
のであり、先の実施例と同様の効果が得られるものであ
る。As described above, in the example of FIG. 4, the control pattern that minimizes the expansion amount of the expansion valve at the time of starting the compressor and then gradually increases the expansion amount is set as the refrigerant at the evaporator outlet or the compressor inlet. Rather than controlling according to the degree of superheat, the time variation of the throttle amount according to the starting characteristics of the device is set in advance, stored in the arithmetic and control unit, and operated according to the control pattern of the stored control procedure. Thus, the same effect as that of the previous embodiment can be obtained.
上述の各実施例によれば、始動後の蒸発温度の低下割合
が小さくでき、蒸発器を有効に活用することができるこ
とから、有効な運転を行うことができる。According to each of the above-described embodiments, the rate of decrease in the evaporation temperature after starting can be reduced, and the evaporator can be effectively used, so that effective operation can be performed.
また、始動時の立上り時間が短縮できることから、空調
機に適用した場合などには快適性が著しく向上される。Further, since the start-up time at the time of starting can be shortened, the comfort is remarkably improved when applied to an air conditioner.
以上述べたように、本発明によれば、圧縮機の起動直
後、蒸発器に流入する冷媒量を多くし、次いで段階的に
冷媒量を減少させるので、蒸発器の機能を活用すること
による冷凍サイクルの立上り時間の減少、および圧縮機
への液戻りによる圧縮機の故障の防止という効果があ
る。また、圧縮機始動時に膨張弁開度が設定時間中に所
定値に達したら、設定時間経過するまで膨張弁開度を変
化させないので、温度センサの時間遅れ等に起因する不
安定現象を防止でき、サイクルの早期安定化が図られる
という効果もある。As described above, according to the present invention, immediately after starting the compressor, the amount of refrigerant flowing into the evaporator is increased, and then the amount of refrigerant is decreased stepwise, so that refrigeration by utilizing the function of the evaporator is performed. This has the effect of reducing the cycle rise time and preventing the failure of the compressor due to liquid return to the compressor. Further, when the expansion valve opening reaches a predetermined value during the set time at the time of starting the compressor, the expansion valve opening is not changed until the set time elapses, so it is possible to prevent an unstable phenomenon due to a time delay of the temperature sensor. Another advantage is that the cycle can be stabilized early.
第1図は、本発明の一実施例に係る冷凍サイクルにおけ
る冷媒流量制御装置の構成図、第2図は、第1図の装置
の電動式膨張弁の制御フローチャートで、(a)は圧縮
機始動時、(b)は定常運転時のフローを示し、第3図
は、圧縮機の始動から定常運転までの膨張弁絞り量,冷
媒温度の変化を示す線図、第4図は、本発明の他の実施
例に係る冷凍サイクルにおける冷媒流量制御装置の制御
パターンを示す線図である。 1……圧縮機、2……凝縮器、3……電動式膨張弁、4
……蒸発器、5……第1の温度センサ、6……第2の温
度センサ、7……演算制御装置。FIG. 1 is a configuration diagram of a refrigerant flow rate control device in a refrigeration cycle according to an embodiment of the present invention, FIG. 2 is a control flowchart of an electric expansion valve of the device of FIG. 1, and (a) is a compressor At the time of start-up, (b) shows the flow during steady operation, FIG. 3 is a diagram showing changes in expansion valve throttle amount and refrigerant temperature from the start of the compressor to steady operation, and FIG. FIG. 6 is a diagram showing a control pattern of a refrigerant flow rate control device in a refrigeration cycle according to another embodiment. 1 ... Compressor, 2 ... Condenser, 3 ... Motorized expansion valve, 4
...... Evaporator, 5 ...... First temperature sensor, 6 ...... Second temperature sensor, 7 ...... Computational control device.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 林 政克 静岡県清水市村松390番地 株式会社日立 製作所機械研究所内 (72)発明者 浅井 節郎 静岡県清水市村松390番地 株式会社日立 製作所清水工場内 (72)発明者 五月女 要 静岡県清水市村松390番地 株式会社日立 製作所清水工場内 (56)参考文献 特開 昭55−116068(JP,A) 特開 昭55−152360(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masakatsu Hayashi, 390 Muramatsu, Shimizu City, Shizuoka Prefecture, Hitachi, Ltd., Mechanical Research Laboratory (72) Inventor, Shiro Asai, 390, Muramatsu, Shimizu City, Shizuoka, Hitachi, Ltd., Shimizu Plant, Hitachi, Ltd. (72) The inventor, May woman, 390 Muramatsu, Shimizu city, Shizuoka prefecture, Shimizu factory, Hitachi, Ltd. (56) References JP 55-116068 (JP, A) JP 55-152360 (JP, A)
Claims (1)
り量が調節可能なパルスモータ駆動式の膨張弁と、蒸発
器とを冷媒配管で順次接続して形成された冷凍サイクル
内を流通する冷媒量を制御する冷媒流量制御方法であっ
て、前記圧縮機の始動後の過渡運転モードと、この過渡
運転モード経過後の定常運転モードとを有し、前記過渡
運転モードは前記圧縮機の始動後の所定時間(τs1)は
前記膨張弁の絞り量を最小とし、その後予め設定した時
間中、第1の温度センサにより検出された前記蒸発器の
冷媒蒸発温度(Te)と第2の温度センサにより検出され
た前記蒸発器出口部あるいは前記圧縮機入口部の冷媒温
度(Ts)との検出温度差を求め、前記検出温度差が設定
温度差(SHa)に近づくよう前記膨張弁の絞り量を所定
時間(τs2)間隔毎に段階的に予め設定された所定の絞
り量まで単調増加させて前記蒸発器の加熱度を徐々に増
加させるとともに、前記予め設定した時間が経過したと
きに前記過渡運転モードから定常運転モードに移行する
ことを特徴とする冷媒流量制御方法。1. A refrigeration cycle formed by sequentially connecting a compressor, a condenser, a pulse motor drive type expansion valve whose throttle amount can be adjusted by an electric signal, and an evaporator with a refrigerant pipe. A method of controlling a refrigerant flow rate for controlling the amount of refrigerant to be used, which has a transient operation mode after the compressor is started, and a steady operation mode after the transient operation mode has elapsed, and the transient operation mode is the compressor. For a predetermined time (τ s1 ) after the start, the expansion amount of the expansion valve is minimized, and thereafter, during a preset time, the refrigerant evaporation temperature (Te) of the evaporator detected by the first temperature sensor and the second Obtain the temperature difference detected with the refrigerant temperature (Ts) at the evaporator outlet or compressor inlet detected by a temperature sensor, and adjust the expansion valve throttle so that the detected temperature difference approaches the set temperature difference (SHa). Quantity at predetermined time intervals (τ s2 ) The heating degree of the evaporator is gradually increased by monotonically increasing to a predetermined throttle amount set stepwise, and when the preset time elapses, the transient operation mode is changed to the steady operation mode. A method for controlling a refrigerant flow rate, which is characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59208284A JPH0772648B2 (en) | 1984-10-05 | 1984-10-05 | Refrigerant flow control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59208284A JPH0772648B2 (en) | 1984-10-05 | 1984-10-05 | Refrigerant flow control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6189455A JPS6189455A (en) | 1986-05-07 |
| JPH0772648B2 true JPH0772648B2 (en) | 1995-08-02 |
Family
ID=16553693
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59208284A Expired - Fee Related JPH0772648B2 (en) | 1984-10-05 | 1984-10-05 | Refrigerant flow control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0772648B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6446539A (en) * | 1987-08-10 | 1989-02-21 | Hitachi Ltd | Method of controlling inverter-loaded air conditioner |
| JPH0833247B2 (en) * | 1988-09-12 | 1996-03-29 | 三菱電機株式会社 | Refrigeration air conditioner |
| KR100382488B1 (en) * | 2000-11-10 | 2003-05-09 | 엘지전자 주식회사 | Method for controlling Linear Expantion Valve of air conditioner with 2 compressors |
| JP2021038907A (en) * | 2019-09-05 | 2021-03-11 | 東芝キヤリア株式会社 | Air conditioner |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55116068A (en) * | 1979-02-28 | 1980-09-06 | Tokyo Shibaura Electric Co | Controller for refrigerating machine |
| JPS55152360A (en) * | 1979-05-17 | 1980-11-27 | Matsushita Electric Industrial Co Ltd | Air conditioner |
| JPS5937419B2 (en) * | 1979-11-28 | 1984-09-10 | 松下電器産業株式会社 | Refrigerant cycle refrigerant flow control device |
-
1984
- 1984-10-05 JP JP59208284A patent/JPH0772648B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6189455A (en) | 1986-05-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0645589B1 (en) | Operation control apparatus for air-conditioner | |
| JP2002071234A (en) | Refrigerator having a plurality of vaporizers | |
| JP2001108323A (en) | Multi-room air conditioner | |
| KR20050015011A (en) | method for controlling system in air conditioner | |
| CN118935832B (en) | A control method for an EVI heat pump | |
| JPH0772648B2 (en) | Refrigerant flow control method | |
| JP2551238B2 (en) | Operation control device for air conditioner | |
| JP3864266B2 (en) | Refrigeration equipment | |
| JP2701598B2 (en) | Freezer refrigerator | |
| JPH09303885A (en) | Refrigerating and air conditioning device | |
| JP2000018777A (en) | Cooler/heater | |
| JPH11132605A (en) | Air conditioner | |
| JPH0544581B2 (en) | ||
| JP2522116B2 (en) | Operation control device for air conditioner | |
| JPH0236019Y2 (en) | ||
| JP2001201198A (en) | Air conditioner control method | |
| JPH0814698A (en) | Operation control device for air conditioner | |
| JPH0719575A (en) | Air conditioner | |
| JP2526435B2 (en) | Refrigeration system operation controller | |
| KR100300581B1 (en) | Cold and heat cycle controll method | |
| JPS59183255A (en) | Air conditioner | |
| KR100585683B1 (en) | Method of landing on inverter heat pump air conditioner | |
| JPH025317Y2 (en) | ||
| JPH0225104Y2 (en) | ||
| KR20000055144A (en) | Method for preventing freezing of the heat exchanger in the air conditioner |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |