JPH07117306B2 - Air conditioner - Google Patents
Air conditionerInfo
- Publication number
- JPH07117306B2 JPH07117306B2 JP63168470A JP16847088A JPH07117306B2 JP H07117306 B2 JPH07117306 B2 JP H07117306B2 JP 63168470 A JP63168470 A JP 63168470A JP 16847088 A JP16847088 A JP 16847088A JP H07117306 B2 JPH07117306 B2 JP H07117306B2
- Authority
- JP
- Japan
- Prior art keywords
- valve opening
- accumulator
- refrigerant
- compressor
- air conditioner
- 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
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- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】 〈産業上の利用分野〉 この発明は、空気調和機に使用される冷媒回路における
返油装置の改良に関するものであり、特に容量制御運転
可能な圧縮機を良好な状態で運転させることを目的とす
る。Description: TECHNICAL FIELD The present invention relates to an improvement of an oil return device in a refrigerant circuit used in an air conditioner, and particularly to a compressor capable of performing capacity control operation in a good state. The purpose is to drive in.
〈従来の技術〉 従来、この種の装置として第5図に示すものがある。図
において、(1)は圧縮機,(2)は四方弁,(3)は
室外熱交換器、(4)は減圧装置,(5)は室内熱交換
器,(6)はアキュムレータ,(6a)は前記アキュムレ
ータ(6)の流出管途中にキリ穴をあけて構成される返
油装置,(11)および(12)はそれぞれガス側延長配管
および液側延長配管である。図中、実線矢印は冷房運転
時の冷媒流れ方向を、また破線矢印は暖房運転時の冷房
流れ方向を示している。<Prior Art> Conventionally, there is an apparatus of this type shown in FIG. In the figure, (1) is a compressor, (2) is a four-way valve, (3) is an outdoor heat exchanger, (4) is a decompressor, (5) is an indoor heat exchanger, (6) is an accumulator, and (6a). ) Is an oil return device constructed by forming a drill hole in the outflow pipe of the accumulator (6), and (11) and (12) are a gas side extension pipe and a liquid side extension pipe, respectively. In the figure, solid arrows indicate the refrigerant flow direction during the cooling operation, and dashed arrows indicate the cooling flow direction during the heating operation.
次に、冷房運転時の動作について説明する。圧縮機
(1)でガス冷媒を圧縮し、吐出された高温高圧のガス
冷媒は、四方弁(2)を介して室外熱交換器(3)に流
入し、室外空気に放熱する一方、冷媒は凝縮して高圧の
液冷媒となり、減圧装置(4)で減圧され、低圧の気液
混合冷媒となって、液側延長配管(12)を介して室内熱
交換器(5)に供給される。室内熱交換器(5)では、
室内空気から採熱して冷房する一方、冷媒は蒸発して低
圧のガス冷媒となり、ガス側延長配管(11)および四方
弁(2)を介してアキュムレータ(6)に流入する。ア
キュムレータ(6)では、室内熱交換器(5)で蒸発し
切れなかった液冷媒とガス冷媒を分離して圧縮機(1)
に吸入させる一方、アキュムレータ(6)の底部に溜ま
っている冷媒と冷凍機油の混合液を返油装置(6a)を介
して圧縮機(1)に吸入させ、圧縮機(1)内部の潤滑
に必要な油量を適正に保持する。Next, the operation during the cooling operation will be described. The high-temperature and high-pressure gas refrigerant that has been compressed and discharged by the compressor (1) flows into the outdoor heat exchanger (3) through the four-way valve (2) and radiates heat to the outdoor air, while the refrigerant is It is condensed to become a high-pressure liquid refrigerant, is decompressed by the decompression device (4), becomes a low-pressure gas-liquid mixed refrigerant, and is supplied to the indoor heat exchanger (5) through the liquid side extension pipe (12). In the indoor heat exchanger (5),
While collecting heat from room air to cool it, the refrigerant evaporates into a low-pressure gas refrigerant, which flows into the accumulator (6) through the gas side extension pipe (11) and the four-way valve (2). In the accumulator (6), the liquid refrigerant and the gas refrigerant that have not completely evaporated in the indoor heat exchanger (5) are separated to separate them from the compressor (1).
While sucking into the compressor (1) through the oil return device (6a), the mixed liquid of the refrigerant and the refrigerating machine oil accumulated at the bottom of the accumulator (6) is sucked into the compressor (1) for lubrication. Keep the required amount of oil properly.
次に、暖房運転時の動作について説明する。圧縮機
(1)でガス冷媒を圧縮し、吐出された高温高圧のガス
冷媒は、四方弁(2)およびガス側延長配管(11)を介
して室内熱交換器(5)に供給され、室内空気に放熱し
て暖房する一方、冷媒は凝縮して高圧の液冷媒となる。
この液冷媒は、液側延長配管(12)を介して減圧装置
(4)に流入し、減圧装置(4)で減圧され低圧の気液
混合冷媒となり室内熱交換器(3)に供給され、室外空
気より採熱して、低圧のガス冷媒となって、四方弁
(2)を介してアキュムレータ(6)に流入する。アキ
ュムレータ(6)では冷房運転時と同様に、ガス冷媒と
液冷媒を分離する一方、圧縮機(1)に必要な冷凍機油
を返油する。Next, the operation during the heating operation will be described. The high-temperature high-pressure gas refrigerant discharged by compressing the gas refrigerant in the compressor (1) is supplied to the indoor heat exchanger (5) through the four-way valve (2) and the gas side extension pipe (11), While radiating heat to the air to heat it, the refrigerant condenses into high-pressure liquid refrigerant.
This liquid refrigerant flows into the pressure reducing device (4) through the liquid side extension pipe (12), is reduced in pressure by the pressure reducing device (4), becomes a low-pressure gas-liquid mixed refrigerant, and is supplied to the indoor heat exchanger (3), Heat is taken from the outdoor air, becomes a low-pressure gas refrigerant, and flows into the accumulator (6) through the four-way valve (2). The accumulator (6) separates the gas refrigerant and the liquid refrigerant, while returning the refrigerating machine oil necessary for the compressor (1), as in the cooling operation.
また、アキュムレータ(6)は冷房運転時と暖房運転時
に必要な冷媒量の差により発生する余剰冷媒量を回収す
る機能がある。つまり、第5図に示す如き冷媒回路構成
の場合、冷房運転時には、液側延長配管(12)内の冷媒
状態は低圧の気液混合冷媒であるため、必要な冷媒量は
比較的少ない。これに対して、暖房運転時には、液側延
長配管(12)内の冷媒状態は高圧の液冷媒となるため、
比重量も大きく、必要な冷媒量が多くなる。従って、冷
房運転時には、多量の冷媒液がアキュムレータ(6)内
に停滞する。この停滞する余剰冷媒量は、延長配管(1
1)および(12)の配管長が長くなる程多くなる。Further, the accumulator (6) has a function of recovering the excess refrigerant amount generated due to the difference between the refrigerant amounts required during the cooling operation and the heating operation. That is, in the case of the refrigerant circuit configuration as shown in FIG. 5, during the cooling operation, the refrigerant state in the liquid side extension pipe (12) is a low-pressure gas-liquid mixed refrigerant, so that the required refrigerant amount is relatively small. On the other hand, during heating operation, the refrigerant state in the liquid side extension pipe (12) becomes high pressure liquid refrigerant,
The specific weight is large and the required amount of refrigerant is large. Therefore, during the cooling operation, a large amount of the refrigerant liquid stays in the accumulator (6). This stagnant amount of excess refrigerant is
The larger the pipe lengths of 1) and (12), the larger.
なお、返油装置(6a)を介して圧縮機(1)に流入する
液冷媒と冷凍機油の混合液流量は簡易的に下記圧力式を
満足するように変動する。The mixed liquid flow rate of the liquid refrigerant and the refrigerating machine oil flowing into the compressor (1) via the oil return device (6a) fluctuates so as to simply satisfy the following pressure equation.
ΔP1+ΔP2=ΔP3 ΔP1:ガス冷媒がアキュム流出管に流入する際に発生
する損失および流出管内の管摩擦損失 ΔP2:アキュムレータ内液面高さによる液柱圧 ΔP3:返油装置(キリ穴)前後に発生する差圧 つまり、ガス冷媒の流速が速くなる程ΔP1が大きくな
り、且つ、アキュムレータ(6)内部の余剰冷媒液量が
多くなる程ΔP2が大きくなるので、返油装置(6a)の
前後差圧ΔP3が大きくなり、結果的に混合液流量が増
加する。従って、冷房運転時には、暖房運転時に比べて
多量の混合液が、圧縮機(1)に流入することになる。ΔP 1 + ΔP 2 = ΔP 3 ΔP 1 : Loss that occurs when the gas refrigerant flows into the accumulator outflow pipe and the pipe friction loss in the outflow pipe ΔP 2 : Liquid column pressure due to the height of the liquid surface in the accumulator ΔP 3 : The oil return device (Differential pressure before and after drilling) That is, ΔP 1 increases as the flow velocity of the gas refrigerant increases, and ΔP 2 increases as the amount of excess refrigerant liquid inside the accumulator (6) increases. The differential pressure ΔP 3 across the oil device (6a) increases, resulting in an increase in the mixed liquid flow rate. Therefore, during the cooling operation, a larger amount of the mixed liquid flows into the compressor (1) than during the heating operation.
以上のように、従来の空気調和機では、アキュムレータ
(6)の返油装置(6a)を一義的に構成しているので、
アキュムレータ(6)内の余剰冷媒液が多い場合には、
返油装置(6a)の返油能力が過大となり、結果的に圧縮
機(1)へ流入する液バック量が多くなり、圧縮機
(1)の故障を誘発したり、圧縮機(1)の運転効率を
低下させたりするという問題があった。なお、前述の如
き、過度の液バックを回避するため、返油装置(6)の
キリ穴サイズを小さくすることが考えられるが、この場
合には、アキュムレータ(6)内の余剰冷媒液が少ない
場合には、十分な返油能力が得られず、アキュムレータ
(6)内に多量の冷凍機油が停滞し、圧縮機(1)の潤
滑が十分でなく事故を引き起こしたりするという問題が
ある。更に、吐出ガス温度が上昇しやすい、高圧縮比運
転時に適度な液バック量が確保されないので、吐出ガス
温度が過熱し、空気調和機の寿命に悪影響を与える。As described above, in the conventional air conditioner, the oil return device (6a) of the accumulator (6) is uniquely configured,
If the excess refrigerant liquid in the accumulator (6) is large,
The oil return capacity of the oil return device (6a) becomes excessively large, and as a result, the amount of liquid back flowing into the compressor (1) increases, causing failure of the compressor (1) or causing the compressor (1) to fail. There was a problem that operating efficiency was reduced. As described above, it is possible to reduce the size of the drill hole of the oil return device (6) in order to avoid excessive liquid back, but in this case, the excess refrigerant liquid in the accumulator (6) is small. In this case, there is a problem that a sufficient oil return capacity cannot be obtained, a large amount of refrigerating machine oil is stagnated in the accumulator (6), and the compressor (1) is not sufficiently lubricated to cause an accident. Furthermore, since the discharge gas temperature is likely to rise and an appropriate amount of liquid back is not ensured during high compression ratio operation, the discharge gas temperature overheats, which adversely affects the life of the air conditioner.
尚、空気調和機に使用する、圧縮機(1)を容量可変形
とした場合には、ガス流速の範囲が広くなり、ガス流速
小の場合は、アキュムレータ(6)内の余剰冷媒液によ
って発生する液柱圧ΔP2の影響度が大きくなるので、
返油装置(6a)を高容量運転時に合わせて選定した場合
には、小容量運転時に極端な液バックとなる。When the compressor (1) used in the air conditioner is of a variable capacity type, the range of the gas flow velocity becomes wide, and when the gas flow velocity is small, it is generated by the excess refrigerant liquid in the accumulator (6). As the influence of the liquid column pressure ΔP 2
If the oil return device (6a) is selected for high-capacity operation, extreme liquid back will occur during small-capacity operation.
この発明は、かかる問題点を解決するためになされたも
ので、アキュムレータ(6)内の余剰冷媒液並びに圧縮
機(1)の運転容量に左右されないで、適度な液バック
と十分な返油量を確保して、圧縮機(1)の運転状態を
良好に維持することを目的とする。The present invention has been made in order to solve such a problem, and is not affected by the operating capacity of the excess refrigerant liquid in the accumulator (6) and the compressor (1), and has a proper liquid level and a sufficient amount of oil return. To maintain the operating condition of the compressor (1) in good condition.
この発明に係わる空気調和機は、圧縮容量調整可能な圧
縮機、四方弁、室外熱交換器、減圧装置、室内熱交換器
及びアキュムレータが配管接続された冷媒回路を有し、
容量制御を行う空気調和機において、上記アキュムレー
タと上記圧縮機を接続する吸入配管と上記アキュムレー
タ底部を接続する返油装置と、上記返油装置と並列関係
に配管接続され、連続的に流量が制御される流量制御装
置と、上記圧縮機の運転容量を制御する運転容量制御手
段と、上記運転容量制御手段による運転容量に応じて上
記流量制御装置の弁開度を制御する弁開度制御手段とを
備え、上記圧縮機の運転容量増加に応じて上記流量制御
装置の弁開度を増加するようにしたものである。An air conditioner according to the present invention has a compressor capable of adjusting a compression capacity, a four-way valve, an outdoor heat exchanger, a pressure reducing device, an indoor heat exchanger, and a refrigerant circuit in which an accumulator is pipe-connected,
In an air conditioner that performs capacity control, a suction pipe that connects the accumulator and the compressor, an oil return device that connects the bottom of the accumulator, and a pipe connection in parallel with the oil return device, and the flow rate is continuously controlled. Flow control device, operating capacity control means for controlling the operating capacity of the compressor, and valve opening control means for controlling the valve opening of the flow control device according to the operating capacity by the operating capacity control means. And the valve opening of the flow rate control device is increased in accordance with an increase in the operating capacity of the compressor.
また、圧縮容量調整可能な圧縮機と四方弁を接続する吐
出配管に設けられた吐出温度検出手段と、上記吐出温度
検出手段による検出温度が所定温度範囲外の時間を計時
する計時手段とを備え、上記計時手段が、上記所定温度
範囲外の時間を所定時間継続して計時した場合、弁開度
制御手段により流量制御装置の弁開度を補正するように
したものである。Further, the discharge temperature detecting means provided in the discharge pipe connecting the compressor capable of adjusting the compression capacity and the four-way valve, and the time measuring means for measuring the time when the temperature detected by the discharge temperature detecting means is outside the predetermined temperature range are provided. When the time measuring means measures the time outside the predetermined temperature range for a predetermined time, the valve opening control means corrects the valve opening of the flow rate control device.
また、冷房運転と暖房運転とを比較して、アキュムレー
タ内の余剰冷媒量が増加する運転モードの流量制御装置
の基準弁開度を余剰冷媒量が減少する運転モードの基準
弁開度より小としたものである。Further, by comparing the cooling operation and the heating operation, the reference valve opening degree of the flow control device in the operation mode in which the excess refrigerant amount in the accumulator increases is smaller than the reference valve opening degree in the operation mode in which the excess refrigerant amount decreases. It was done.
この発明では、圧縮機の運転容量増加に応じて流量制御
装置の弁開度を増加する。また、吐出温度が設定温度範
囲外を所定時間継続した場合に、上記流量制御装置の弁
開度を補正する。また、運転モードによりアキュムレー
タ内の余剰冷媒量が変わる場合、上記流量制御装置の基
準弁開度をそれに応じて変える。According to the present invention, the valve opening degree of the flow rate control device is increased according to the increase of the operating capacity of the compressor. Further, when the discharge temperature is out of the set temperature range for a predetermined time, the valve opening of the flow rate control device is corrected. Also, when the amount of surplus refrigerant in the accumulator changes depending on the operation mode, the reference valve opening of the flow rate control device is changed accordingly.
第1図は、この発明の一実施例による空気調和機の全体
構成図である。図において、(1)(2)(3)(4)
(5)及び(11)(12)は第5図に示す従来の空気調和
機と同様のものである。(6)はアキュムレータであ
り、流出管は上部に位置している。(7)はアキュムレ
ータ(6)底部と吸入配管(10)に配管接続された返油
装置であり、毛細管あるいは管オリフィスにより構成さ
れると共に、流量特性的には圧縮機(1)の最小運転容
量に合致させている。(8)は返油装置(7)と並列に
配管接続された流量制御装置である電気式膨張弁であ
り、電気信号により通過流量が変更できる。(13)は圧
縮機(1)と四方弁(2)を接続する吐出配管(9)部
に設けられた吐出温度検出手段、(23)は前記吐出温度
検出手段(13)による検出温度が設定温度範囲外のとき
時間を計時する計時手段、(22)は室内熱交換器(5)
部における温度状態並びに運転モードにより圧縮機
(1)の運転容量を決定する運転容量制御手段、(21)
は上記運転容量制御手段(22)および計時手段(23)の
出力信号に基づき、電気式膨張弁(8)の弁開度を制御
する弁開度制御手段である。FIG. 1 is an overall configuration diagram of an air conditioner according to an embodiment of the present invention. In the figure, (1) (2) (3) (4)
(5), (11) and (12) are the same as those of the conventional air conditioner shown in FIG. (6) is an accumulator, and the outflow pipe is located in the upper part. Reference numeral (7) is an oil return device connected to the bottom of the accumulator (6) and the suction pipe (10), and is composed of a capillary tube or pipe orifice, and in terms of flow characteristics, the minimum operating capacity of the compressor (1). To match. (8) is an electric expansion valve which is a flow control device connected in parallel with the oil return device (7), and the passing flow rate can be changed by an electric signal. (13) is a discharge temperature detecting means provided in a discharge pipe (9) connecting the compressor (1) and the four-way valve (2), and (23) is a temperature detected by the discharge temperature detecting means (13). Time measuring means for measuring time when the temperature is out of the temperature range, (22) is an indoor heat exchanger (5)
Capacity control means for determining the operating capacity of the compressor (1) according to the temperature state and operating mode in the section, (21)
Is a valve opening degree control means for controlling the valve opening degree of the electric expansion valve (8) based on the output signals of the operating capacity control means (22) and the timing means (23).
尚、図中実線矢印は冷房運転時の冷媒流れ方向を示し、
破線矢印は暖房運転時の冷媒流れ方向を示す。冷房運転
時並びに暖房運転時の冷媒側の動作については第5図に
示す従来の空気調和機と全く同様なので説明を省略し、
電気式膨張弁(8)の動作について説明する。In addition, the solid line arrow in the figure indicates the refrigerant flow direction during the cooling operation,
The dashed arrow indicates the direction of refrigerant flow during heating operation. The operation on the refrigerant side during the cooling operation and the heating operation is exactly the same as that of the conventional air conditioner shown in FIG.
The operation of the electric expansion valve (8) will be described.
第2図は、弁開度制御手段(21)による電気式膨張弁
(8)の基準開度Saを圧縮機(1)の運転容量Qに応じ
て設定する特性図であり、(25)は冷房運転時の基準開
度線図,(26)は暖房運転時の基準開度線図を示し、圧
縮機(1)の運転容量Qが所定の値以下では基準開度Sa
が0となるように設定される。返油装置(7)、並びに
電気式膨張弁(8)を介して流れる冷媒液と冷凍機油の
混合液流量は従来の空気調和機同様に、簡易的に下記圧
力式を満足するだけの流量となる。FIG. 2 is a characteristic diagram for setting the reference opening degree Sa of the electric expansion valve (8) by the valve opening control means (21) according to the operating capacity Q of the compressor (1), and (25) is The reference opening diagram during cooling operation, (26) shows the reference opening diagram during heating operation, and when the operating capacity Q of the compressor (1) is less than a predetermined value, the reference opening Sa
Is set to 0. Like the conventional air conditioner, the flow rate of the mixed liquid of the refrigerant liquid and the refrigerating machine oil flowing through the oil return device (7) and the electric expansion valve (8) is simply enough to satisfy the following pressure formula. Become.
ΔP1+ΔP2=ΔP3 ΔP1:ガス冷媒がアキュムレータ流出管に流入する際
に発生する損失および流出管内の管摩擦損失 ΔP2:アキュムレータ内液面高さによる液柱圧 ΔP3:返油装置(7)、または電気式膨張弁(8)前
後に発生する差圧 つまり、従来の空気調和機で説明した通り、冷房運転時
には液側延長配管(12)内の冷媒状態が低圧の気液混合
冷媒となるため、アキュムレータ(6)内部に多量の余
剰冷媒液が保持され、液面高さにより発生する液柱圧Δ
P2が大となっている。この状態で、圧縮機(1)の運
転容量Qが比較的小さい場合には、電気式膨張弁(8)
の基準開度Saを0と設定し、冷媒液と冷凍機油の混合液
は返油装置(7)のみにより圧縮機(1)に供給され、
且つ返油装置(7)を通過する混合液流量が適正となる
よう、返油装置(7)の流路抵抗を選定している。圧縮
機(1)の運転容量Qが増加した場合には、冷媒ガス流
速が増大するので、アキュムレータ(6)の流出管内に
発生する損失ΔP1が増大する。この結果返油装置
(7)に発生する差圧ΔP3が増加し混合液の流量が増
加する。しかしながら、返油装置(7)の混合液流量は
圧縮機(1)の運転容量Qに対し第3図に示す如き特性
となるので、圧縮機(1)の運転容量Qが増加した場合
には、混合液流量の割合が小となり、相対的に流量不足
となる。従って、第2図に示す如く、運転容量Qの増加
に応じて、電気式膨張弁(8)の弁開度を増大させて、
電気式膨張弁(8)を通過する冷媒液と冷凍機油の混合
液量を変化させ、あらゆる運転容量Qにおいて、適度な
返油並びに液バック量を達成するものである。ΔP 1 + ΔP 2 = ΔP 3 ΔP 1 : Loss generated when gas refrigerant flows into the accumulator outflow pipe and pipe friction loss in the outflow pipe ΔP 2 : Liquid column pressure due to liquid level in accumulator ΔP 3 : Returning device (7) or the differential pressure generated before and after the electric expansion valve (8) In other words, as explained in the conventional air conditioner, during the cooling operation, the refrigerant state in the liquid side extension pipe (12) is a low pressure gas-liquid mixture. Since it becomes a refrigerant, a large amount of excess refrigerant liquid is retained inside the accumulator (6), and the liquid column pressure Δ caused by the liquid level height Δ
P 2 is large. In this state, when the operating capacity Q of the compressor (1) is relatively small, the electric expansion valve (8)
The reference opening Sa of is set to 0, and the mixed liquid of the refrigerant liquid and the refrigerating machine oil is supplied to the compressor (1) only by the oil return device (7),
In addition, the flow path resistance of the oil return device (7) is selected so that the flow rate of the mixed liquid passing through the oil return device (7) becomes appropriate. When the operating capacity Q of the compressor (1) increases, the refrigerant gas flow velocity increases, so the loss ΔP 1 generated in the outflow pipe of the accumulator (6) increases. As a result, the differential pressure ΔP 3 generated in the oil return device (7) increases and the flow rate of the mixed liquid increases. However, since the mixed liquid flow rate of the oil return device (7) has characteristics as shown in FIG. 3 with respect to the operating capacity Q of the compressor (1), when the operating capacity Q of the compressor (1) increases. The ratio of the mixed liquid flow rate becomes small and the flow rate becomes relatively insufficient. Therefore, as shown in FIG. 2, the valve opening of the electric expansion valve (8) is increased in accordance with the increase of the operating capacity Q,
The amount of the mixed liquid of the refrigerant liquid and the refrigerating machine oil passing through the electric expansion valve (8) is changed to achieve an appropriate oil return and liquid back amount at any operating capacity Q.
また、暖房運転時には、液側延長配管(12)内の冷媒状
態が高圧の液冷媒となるため、アキュムレータ(6)内
部の冷媒液は少量となり、液面高さによる液柱圧ΔP2
が冷房運転時に比べて小となり、返油装置(7)の返油
能力が小となるので、冷媒液と冷凍機油の混合液流量が
小さくなる。従って、暖房運転時には、電気式膨張弁
(8)の基準開度Saを第2図の如く冷房運転時に対して
大き目に設定し、適度な返油並びに液バック量が得られ
るように設定している。Further, during the heating operation, the state of the refrigerant inside the liquid side extension pipe (12) becomes a high-pressure liquid refrigerant, so that the refrigerant liquid inside the accumulator (6) becomes small and the liquid column pressure ΔP 2 due to the liquid level height.
Becomes smaller than that during the cooling operation, and the oil return capacity of the oil return device (7) becomes small, so that the flow rate of the mixed liquid of the refrigerant liquid and the refrigerating machine oil becomes small. Therefore, during the heating operation, the reference opening degree Sa of the electric expansion valve (8) is set to be larger than that during the cooling operation as shown in FIG. 2 so that an appropriate amount of oil return and liquid back amount can be obtained. There is.
尚、前述の如き返油・液バック量の調整は、アキュムレ
ータ(6)内の余剰液量に依存するため、室外空気温度
・室内空気温度条件あるいは延長配管(11)(12)の長
さによっては必ずしも適正値を設定できないことも想定
されているので、冷媒液と冷凍機油の混合液流量により
温度変化する吐出配管(9)部の温度を吐出温度検出手
段(13)により検出し、設定温度範囲外となっている時
間を計時手段(23)により計時し、吐出温度が設定温度
以上を所定時間継続した場合には、混合液流量不足と判
定し、電気式膨張弁(8)の弁開度を増加補正する。ま
た、吐出温度が設定温度以下を所定時間継続した場合に
は、混合液流量過多と判定し、電気式膨張弁(8)の弁
開度を減少補正する。尚、前述の弁開度補正量は、冷房
運転時と暖房運転時における電気式膨張弁(8)の開度
による混合液流量変化率が異なるので、(同一弁開度変
化でも、液柱圧ΔP2の大きな冷房運転時には流量変化
が大)運転モードにより変更している。The adjustment of the amount of oil return and liquid back as described above depends on the amount of surplus liquid in the accumulator (6). Therefore, depending on the outdoor air temperature / indoor air temperature conditions or the length of the extension pipes (11) (12). Since it is assumed that an appropriate value cannot always be set, the discharge temperature detecting means (13) detects the temperature of the discharge pipe (9) that changes depending on the flow rate of the mixed liquid of refrigerant liquid and refrigerating machine oil, and When the time outside the range is measured by the time measuring means (23) and the discharge temperature continues to be equal to or higher than the set temperature for a predetermined time, it is judged that the mixed liquid flow rate is insufficient and the valve of the electric expansion valve (8) is opened. Correct the increase. When the discharge temperature continues to be equal to or lower than the set temperature for a predetermined time, it is determined that the flow rate of the mixed liquid is excessive and the valve opening degree of the electric expansion valve (8) is corrected to be decreased. Note that the above-mentioned valve opening correction amount is different from the above because the rate of change in the mixed liquid flow rate depending on the opening of the electric expansion valve (8) during cooling operation and heating operation is different ( The flow rate changes greatly during cooling operation with a large ΔP 2 ) It is changed according to the operation mode.
次に、本実施例に基づく空気調和機の電気式膨張弁
(8)の弁開度制御手段(21)の制御状態を第4図に示
すフローチャートにより説明する。ステップ(41)で圧
縮機(1)が起動し、ステップ(42)では運転容量制御
手段(22)により圧縮機(1)の運転容量を決定して所
定運転容量で運転し、ステップ(43)で冷房運転と暖房
運転を判別して第2図に示す基準開度線図(25)(26)
に基づき、圧縮機(1)の運転容量Qに応じた基準開度
Saをステップ(44)あるいは(45)で設定する。ステッ
プ(46)では吐出温度検出手段(13)による検出温度が
所定温度範囲内か否かを判別して、所定温度範囲内の場
合には、ステップ(60)で計時手段(23)のタイマーを
リセットし、ステップ(61)に進み、開度補正量ΔSを
0として、ステップ(59)で電気式膨張弁(8)の弁開
度Sを基準開度Saとして出力する。一方、ステップ(4
6)で吐出温度が所定温度範囲外となった場合には、ス
テップ(47)(48)と進み、計時手段(23)のタイマー
をセットして、ステップ(49)で所定温度範囲外の時間
が所定時間経過したか否かを判別し、所定時間経過して
いない場合にはステップ(59)で電気式膨張弁(8)の
弁開度Sを基準開度Saのままとする。吐出温度が所定温
度範囲外で所定時間継続した場合には、ステップ(50)
に進み、タイマーをリセットして、ステップ(51)に進
み、吐出温度が第1の所定温度以上の場合には、ステッ
プ(52)(53)(54)に進み、冷房運転時には開度補正
量ΔSにΔS1を、暖房運転時には開度補正量ΔSにΔ
S2を加えて、ステップ(55)(59)に進んで、電気式
膨張弁(8)の弁開度Sを基準開度Saに対してΔS+Δ
S1,またはΔS+ΔS2だけ増加補正する。この開度補
正量は、冷房運転時にはアキュムレータ(6)の液量が
大のため、ΔS1<ΔS2となっている。また、吐出温度
が第2の所定温度以下の場合には、(ただし、第1の所
定温度>第2の所定温度)ステップ(51)(55)(56)
(57)(58)と進んで、冷房運転時には開度補正量ΔS
からΔS1を、暖房運転時には開度補正量ΔSからΔS2
を引いて、ステップ(59)に進んで、電気式膨張弁
(8)の弁開度Sを基準開度Saに対してΔSだけ減少補
正する。尚タイマーカウント中に、吐出温度が予定温度
範囲内に入った場合には、ステップ(46)でステップ
(60)に進んで開度補正量ΔSを0として補正をキャン
セルする。また、吐出温度が予定温度範囲外に継続して
いる場合には、所定時間ごとに、ステップ(53)(54)
あるいはステップ(57)(58)により開度補正を繰り返
す。Next, the control state of the valve opening control means (21) of the electric expansion valve (8) of the air conditioner according to this embodiment will be described with reference to the flowchart shown in FIG. In step (41), the compressor (1) is started, and in step (42), the operating capacity control means (22) determines the operating capacity of the compressor (1) to operate at a predetermined operating capacity, and then in step (43). Distinguish between cooling operation and heating operation with the standard opening diagram (25) (26) shown in Fig. 2.
Based on the standard opening degree according to the operating capacity Q of the compressor (1)
Set Sa in step (44) or (45). In step (46), it is judged whether or not the temperature detected by the discharge temperature detecting means (13) is within the predetermined temperature range. If it is within the predetermined temperature range, the timer of the time measuring means (23) is set in step (60). After resetting and proceeding to step (61), the opening correction amount ΔS is set to 0, and the valve opening S of the electric expansion valve (8) is output as the reference opening Sa in step (59). On the other hand, step (4
If the discharge temperature is out of the specified temperature range in 6), proceed to steps (47) and (48), set the timer of the time measuring means (23), and set the time outside the specified temperature range in step (49). It is determined whether or not a predetermined time has elapsed, and if the predetermined time has not elapsed, the valve opening S of the electric expansion valve (8) is left at the reference opening Sa in step (59). If the discharge temperature is outside the specified temperature range and continues for the specified time, step (50)
To reset the timer and proceed to step (51). If the discharge temperature is equal to or higher than the first predetermined temperature, proceed to steps (52) (53) (54). ΔS is set to ΔS 1 , and the opening correction amount ΔS is set to ΔS during heating operation.
After adding S 2 , the process proceeds to steps (55) and (59), where the valve opening S of the electric expansion valve (8) is ΔS + Δ with respect to the reference opening Sa.
Increase correction by S 1 or ΔS + ΔS 2 . The opening correction amount is ΔS 1 <ΔS 2 because the amount of liquid in the accumulator (6) is large during the cooling operation. When the discharge temperature is equal to or lower than the second predetermined temperature (where, the first predetermined temperature> the second predetermined temperature), steps (51) (55) (56)
(57) Go to (58), the opening correction amount ΔS during cooling operation
From ΔS 1 and from the opening correction amount ΔS to ΔS 2 during heating operation.
And proceeds to step (59) to correct the valve opening S of the electric expansion valve (8) by ΔS with respect to the reference opening Sa. When the discharge temperature is within the predetermined temperature range during the timer counting, the process proceeds to step (60) at step (46) to set the opening correction amount ΔS to 0 and cancel the correction. If the discharge temperature continues to be outside the planned temperature range, the steps (53) and (54) are performed at predetermined time intervals.
Alternatively, the opening degree correction is repeated by steps (57) and (58).
なお、この実施例においては、基準開度Saおよび開度補
正量ΔSの設定を冷房運転時に比べて暖房運転時に大き
くするようにしているが、室内側に減圧装置(4)を設
けた空気調和機の場合には、暖房運転時にアキュムレー
タ(6)内の余剰冷媒が増加するので、暖房運転時の基
準開度S2および開度補正量ΔS2を小さくする必要があ
る。In this embodiment, the setting of the reference opening Sa and the opening correction amount ΔS is set to be larger during the heating operation than during the cooling operation. However, the air conditioner in which the decompression device (4) is provided on the indoor side is used. In the case of the air conditioner, since the excess refrigerant in the accumulator (6) increases during the heating operation, it is necessary to reduce the reference opening S 2 and the opening correction amount ΔS 2 during the heating operation.
また、この実施例においては、返油装置(7)をアキュ
ムレータ(6)の外部に設けているが、従来の空気調和
機同様にアキュムレータ(6)内部の流出管に設けたキ
リ穴で構成してもよい。Further, in this embodiment, the oil return device (7) is provided outside the accumulator (6). However, like the conventional air conditioner, the oil return device (7) is provided with a drill hole provided in the outflow pipe inside the accumulator (6). May be.
返油装置と並列関係に配管接続され、連続的に流量が制
御される流量制御装置と、圧縮機の運転容量を制御する
運転容量制御手段と、上記運転容量制御手段による運転
容量に応じて上記流量制御装置の弁開度を制御する弁開
度制御手段とを備え、上記圧縮機の運転容量増加に応じ
て上記流量制御装置の弁開度を増加するようにしたの
で、圧縮容量調整可能な圧縮機の圧縮容量に応じて圧縮
機へ戻す油量と冷媒液量を無段階に、連続的に制御で
き、運転容量に関係なく、適正な返油量及び液バック量
が得られ圧縮機の圧縮容量制御運転が良好に行われる。A flow rate control device connected in parallel with the oil return device to control the flow rate continuously, operating capacity control means for controlling the operating capacity of the compressor, and the operating capacity control means for operating capacity Since the valve opening control means for controlling the valve opening of the flow control device is provided and the valve opening of the flow control device is increased in accordance with the increase in the operating capacity of the compressor, the compression capacity can be adjusted. Depending on the compression capacity of the compressor, the amount of oil returned to the compressor and the amount of refrigerant liquid can be continuously controlled steplessly, and an appropriate amount of oil return and liquid back amount can be obtained regardless of the operating capacity. The compression capacity control operation is performed well.
また、計時手段が、吐出配管の温度が所定温度範囲外の
時間を所定時間継続して計時した場合、弁開度制御手段
により流量制御装置の弁開度を補正することにより、返
油量及び液バック量が一時的な温度変動に影響されず
に、一層適正値に設定できる。Further, when the time measuring means measures the time of the temperature of the discharge pipe being out of the predetermined temperature range for a predetermined period of time, the valve opening control means corrects the valve opening of the flow rate control device to obtain the oil return amount and The liquid back amount can be set to a more appropriate value without being affected by temporary temperature fluctuations.
また、アキュムレータ内の余剰冷媒量が増加する運転モ
ードの流量制御装置の基準弁開度を余剰冷媒量が減少す
る運転モードの基準弁開度より小とすることにより、運
転モードによりアキュムレータ内の余剰冷媒流量が変わ
る場合、流量制御装置の基準弁開度をそれに応じて変え
ているので、運転モードに左右されないで適正な返油量
及び液バック量が得られる。Further, by setting the reference valve opening of the flow control device in the operation mode in which the excess refrigerant amount in the accumulator increases to be smaller than the reference valve opening in the operation mode in which the excess refrigerant amount decreases, the excess in the accumulator depending on the operation mode. When the refrigerant flow rate changes, the reference valve opening degree of the flow rate control device is changed accordingly, so that an appropriate oil return amount and liquid back amount can be obtained regardless of the operation mode.
第1図は、この発明の一実施例による空気調和機の全体
構成図、第2図は同じく電気式膨張弁の弁開度特性図、
第3図は同じく返油装置の流量特性図、第4図は同じく
電気式膨張弁の弁開度制御手段による制御フローチャー
ト、第5図は従来の空気調和機の全体構成図である。 図中、(1)は圧縮機、(2)は四方弁、(3)は室外
熱交換器、(4)は減圧装置、(5)は室内熱交換器、
(6)はアキュムレータ、(7)は返油装置、(8)は
電気式膨張弁、(13)は吐出温度検出手段、(21)は弁
開度制御手段、(22)は運転容量制御手段、(23)は計
時手段である。 なお、各図中同一符号は、同一または相当部分を示す。FIG. 1 is an overall configuration diagram of an air conditioner according to an embodiment of the present invention, and FIG. 2 is a valve opening characteristic diagram of the same electric expansion valve,
FIG. 3 is a flow rate characteristic diagram of the oil return device, FIG. 4 is a control flow chart by the valve opening control means of the electric expansion valve, and FIG. 5 is an overall configuration diagram of a conventional air conditioner. In the figure, (1) is a compressor, (2) is a four-way valve, (3) is an outdoor heat exchanger, (4) is a decompression device, (5) is an indoor heat exchanger,
(6) is an accumulator, (7) is an oil return device, (8) is an electric expansion valve, (13) is discharge temperature detection means, (21) is valve opening control means, and (22) is operating capacity control means. , (23) is a timekeeping means. The same reference numerals in the drawings indicate the same or corresponding parts.
Claims (3)
熱交換器、減圧装置、室内熱交換器及びアキュムレータ
が配管接続された冷媒回路を有し、容量制御を行う空気
調和機において、上記アキュムレータと上記圧縮機を接
続する吸入配管と上記アキュムレータ底部を接続する返
油装置と、上記返油装置と並列関係に配管接続され、連
続的に流量が制御される流量制御装置と、上記圧縮機の
運転容量を制御する運転容量制御手段と、上記運転容量
制御手段による運転容量に応じて上記流量制御装置の弁
開度を制御する弁開度制御手段とを備え、上記圧縮機の
運転容量増加に応じて上記流量制御装置の弁開度を増加
するようにしたことを特徴とする空気調和機。1. An air conditioner which has a refrigerant circuit in which a compressor capable of adjusting a compression capacity, a four-way valve, an outdoor heat exchanger, a pressure reducing device, an indoor heat exchanger and an accumulator are connected by piping, and which controls a capacity, A suction pipe that connects the accumulator and the compressor, an oil return device that connects the bottom of the accumulator, a pipe connection in parallel with the oil return device, and a flow rate control device that continuously controls the flow rate, and the compression unit. An operating capacity control means for controlling the operating capacity of the compressor, and a valve opening control means for controlling the valve opening of the flow rate control device according to the operating capacity by the operating capacity control means. An air conditioner characterized in that the valve opening degree of the flow rate control device is increased according to the increase.
する吐出配管に設けられた吐出温度検出手段と、上記吐
出温度検出手段による検出温度が所定温度範囲外の時間
を計時する計時手段とを備え、上記計時手段が、上記所
定温度範囲外の時間を所定時間継続して計時した場合、
弁開度制御手段により流量制御装置の弁開度を補正する
ことを特徴とする特許請求の範囲第1項記載の空気調和
機。2. A discharge temperature detecting means provided in a discharge pipe connecting a compressor capable of adjusting a compression capacity and a four-way valve, and a time measuring means for measuring a time when a temperature detected by the discharge temperature detecting means is outside a predetermined temperature range. And, when the time measuring means continuously measures a time outside the predetermined temperature range for a predetermined time,
The air conditioner according to claim 1, wherein the valve opening control means corrects the valve opening of the flow control device.
ムレータ内の余剰冷媒量が増加する運転モードの流量制
御装置の基準弁開度を余剰冷媒量が減少する運転モード
の基準弁開度より小とすることを特徴とする特許請求の
範囲第1項または第2項記載の空気調和機。3. A cooling operation and a heating operation are compared with each other, and a reference valve opening of a flow control device in an operation mode in which the amount of surplus refrigerant in the accumulator increases and a reference valve opening in an operation mode in which the amount of surplus refrigerant decreases. The air conditioner according to claim 1 or 2, wherein the air conditioner has a smaller size.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63168470A JPH07117306B2 (en) | 1988-07-05 | 1988-07-05 | Air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63168470A JPH07117306B2 (en) | 1988-07-05 | 1988-07-05 | Air conditioner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0217360A JPH0217360A (en) | 1990-01-22 |
| JPH07117306B2 true JPH07117306B2 (en) | 1995-12-18 |
Family
ID=15868704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63168470A Expired - Lifetime JPH07117306B2 (en) | 1988-07-05 | 1988-07-05 | Air conditioner |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07117306B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5213538B2 (en) * | 2008-06-19 | 2013-06-19 | 三菱電機株式会社 | Renewal method of refrigeration cycle equipment |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5270319U (en) * | 1975-11-20 | 1977-05-25 | ||
| JPS6363660U (en) * | 1986-10-15 | 1988-04-27 | ||
| JPH01167555U (en) * | 1988-05-10 | 1989-11-24 |
-
1988
- 1988-07-05 JP JP63168470A patent/JPH07117306B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0217360A (en) | 1990-01-22 |
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