JPS5845450A - Refrigerant amount adjustment device in refrigeration equipment - Google Patents
Refrigerant amount adjustment device in refrigeration equipmentInfo
- Publication number
- JPS5845450A JPS5845450A JP56143662A JP14366281A JPS5845450A JP S5845450 A JPS5845450 A JP S5845450A JP 56143662 A JP56143662 A JP 56143662A JP 14366281 A JP14366281 A JP 14366281A JP S5845450 A JPS5845450 A JP S5845450A
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- amount adjustment
- refrigerant amount
- load
- adjustment container
- 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.)
- Granted
Links
Landscapes
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は、負荷の変化に対して、冷媒回路中を流れる冷
媒循環量を変化させ、負荷に応じて最高冷凍能力を発揮
させることができる冷媒量調節装置の改良に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a refrigerant amount adjusting device that can change the amount of refrigerant circulating in a refrigerant circuit in response to a change in load, and can exhibit the maximum refrigerating capacity according to the load. It is something.
従来、冷媒量調節装置を備えた冷凍装置は、第1図に示
すように、圧縮機a、凝縮器す、絞り装置C9蒸発器d
をそれぞれ環状に連結し、冷媒量調節容器eを絞り装置
Cの途中の接続位置qに、あるいは、絞り装置Cと蒸発
器dとの間に連結し、さらに、圧縮機aと蒸発器dとを
連結する吸入管fを冷媒量調節容器eに貫通させた構成
が知られている。Conventionally, a refrigeration system equipped with a refrigerant amount adjustment device has a compressor a, a condenser S, a throttle device C9, an evaporator d, as shown in FIG.
are connected in an annular manner, and the refrigerant amount adjusting container e is connected to a connection position q in the middle of the expansion device C, or between the expansion device C and the evaporator d, and the compressor a and the evaporator d are connected to each other. A known configuration is known in which a suction pipe f connecting the refrigerant amount adjusting container e is penetrated through the refrigerant amount adjusting container e.
このような構成にした場合、絞り装置Cと冷媒量調節容
器eとの接続位置qの冷媒は、気液二相の飽和状態であ
る。だから、もし、吸入管fが冷媒量調節容器eを貫通
していなければ、冷媒量調節容器eの内部の冷媒状態は
、絞り装置Cと冷媒量調節容器eとの接続位置qの冷媒
と同じ飽和状態になる。しかし、吸入管量が冷媒量調節
容器eを貫通している場合には、通常、吸入管fの温度
は絞り装置Cと冷媒量調節容器eとの一接続位署qの温
度よりも低いため、冷媒量調節容器eの内部の冷媒の一
部が凝縮する。よって、絞シ装置Cと冷媒量調節容器e
との接続位置qの冷媒の湿り度よりも、冷媒量調節容器
eの内部の冷媒の湿り度の方が大きくなる。つまり、吸
入管fの温度の方が、前記接続位置qの温度よりも低い
場合には、冷媒量調節容器eに冷媒が蓄積されるだけで
ある。In such a configuration, the refrigerant at the connection position q between the expansion device C and the refrigerant amount adjustment container e is in a gas-liquid two-phase saturated state. Therefore, if the suction pipe f does not penetrate the refrigerant amount adjustment container e, the state of the refrigerant inside the refrigerant amount adjustment container e is the same as that of the refrigerant at the connection position q between the expansion device C and the refrigerant amount adjustment container e. Become saturated. However, when the suction pipe amount passes through the refrigerant amount adjustment container e, the temperature of the suction pipe f is usually lower than the temperature at the connection point q between the throttle device C and the refrigerant amount adjustment container e. , a part of the refrigerant inside the refrigerant amount adjustment container e condenses. Therefore, the throttling device C and the refrigerant amount adjustment container e
The humidity of the refrigerant inside the refrigerant amount adjustment container e is greater than the humidity of the refrigerant at the connection position q. That is, when the temperature of the suction pipe f is lower than the temperature of the connection position q, the refrigerant is simply accumulated in the refrigerant amount adjustment container e.
上述した冷媒量調節容器eの内部の冷媒状態の負荷に対
する変化を、第2図を用いて説明する。The change in the state of the refrigerant inside the refrigerant amount adjusting container e described above with respect to the load will be explained using FIG. 2.
冷媒量調節容器eの熱収支を考える場合、その主な熱量
は、冷媒量調節容器eの周囲の空気からの熱伝達によっ
て冷媒量調節容器eに侵入する熱量と、冷媒量調節容器
eを貫通している吸入管fによって冷媒量調節容器eか
ら奪われる熱量とがある。第2図は、横軸に冷凍装置の
負荷の大きさをとり、縦軸に冷媒量調節容器eへの侵入
熱量をとって、冷凍装置の負荷変動に対する冷媒量調節
容器eの熱収支を説明したものである。ただし、侵入熱
量が負ということは、冷媒量調節容器eより熱量が奪わ
れることを意味している。第2図において、曲線q1は
負荷に対する周囲空気から侵入する熱量の変化をあられ
し、曲線q2は負荷に対する吸入管fから侵入する熱量
の変化をあられしている。そして、冷媒量調節容器eに
侵入する全熱量は、qlと92を加えた熱量になり、こ
の全侵入熱量は曲線q3であられしている。ここで、曲
線q3上の点Xは、冷媒量調節容器eへの侵入熱量がな
いことを意味している。When considering the heat balance of the refrigerant amount adjustment container e, the main amount of heat is the amount of heat that enters the refrigerant amount adjustment container e by heat transfer from the air around the refrigerant amount adjustment container e, and the amount of heat that penetrates the refrigerant amount adjustment container e. There is an amount of heat removed from the refrigerant amount adjustment container e by the suction pipe f. Fig. 2 shows the heat balance of the refrigerant amount adjustment container e with respect to load fluctuations of the refrigeration equipment, with the horizontal axis representing the magnitude of the load on the refrigeration system and the vertical axis representing the amount of heat entering the refrigerant amount adjustment container e. This is what I did. However, the fact that the amount of heat entering is negative means that the amount of heat is taken away from the refrigerant amount adjustment container e. In FIG. 2, a curve q1 shows the change in the amount of heat entering from the ambient air with respect to the load, and a curve q2 shows the change in the amount of heat entering from the suction pipe f with respect to the load. The total amount of heat that enters the refrigerant amount adjustment container e is the sum of ql and 92, and this total amount of heat that enters is represented by a curve q3. Here, the point X on the curve q3 means that there is no amount of heat entering the refrigerant amount adjustment container e.
ところで、冷媒量調節容器eが冷媒量の調節機能を果た
す場合は、この点Xであられされる負荷をほぼ中心とし
て、その前後のある範囲の負荷変動の場合だけである。By the way, the case where the refrigerant amount adjusting container e performs the function of adjusting the refrigerant amount is only when the load at point X is approximately the center and the load fluctuates within a certain range before and after it.
なぜなら、点Xの一負荷よりも負荷がかなり大きくなる
と、冷媒量調節容器eの内部の冷媒は常に過熱蒸気の状
態となり、負荷変動があっても冷媒量調節容器eの内部
の冷媒の過熱度が変化するだけであって、冷媒量調節容
器eの内部に蓄積される冷媒の質量には、はとんど変化
がない。逆に、点Xの負荷よりも負荷がかなり小さくな
ると、冷媒量調節容器eの内部?冷媒は常に過冷却液状
態となり、負荷変動があっても、冷媒量調節容器eの内
部の冷媒の過冷却度が変化するだけであって、冷媒量調
節容器eの内部に蓄積される冷媒の質量にはほとんど変
化がない。しかし、冷凍装置が使用される通常の負荷の
範囲は、第2図の点mと点nで示される範囲である。つ
まり、冷凍装置が使用される通常の負荷範囲は、点Xで
あられされる負荷よりも、かなり低いということになる
。This is because when the load becomes considerably larger than one load at point The mass of the refrigerant accumulated inside the refrigerant amount adjustment container e does not change at all. Conversely, if the load becomes much smaller than the load at point X, the inside of the refrigerant amount adjustment container e? The refrigerant is always in a supercooled liquid state, and even if there is a load change, only the degree of supercooling of the refrigerant inside the refrigerant amount adjustment container e changes, and the amount of refrigerant accumulated inside the refrigerant amount adjustment container e changes. There is almost no change in mass. However, the typical load range in which the refrigeration system is used is the range shown by points m and n in FIG. This means that the normal load range in which the refrigeration system is used is significantly lower than the load experienced at point X.
上記説明より明らかなように、結局、冷凍装置が使用さ
れる通常の負荷範囲では、従来の冷媒量調節容器eの内
部は過冷却液で占められ、負荷が極端に大きな範囲でし
か冷媒量調節機能を果たさなく、冷凍装置が使用される
通常の負荷の範囲では、はとんど冷媒量の調節機能を果
たさないという欠点があった。特に低負荷時には、圧縮
機に液戻りが生じるという短所があった。As is clear from the above explanation, in the normal load range in which the refrigeration system is used, the interior of the conventional refrigerant amount adjustment container e is occupied by supercooled liquid, and the refrigerant amount is adjusted only in an extremely large load range. It has the disadvantage that it does not perform the function of adjusting the amount of refrigerant within the normal load range in which the refrigeration system is used. Particularly at low loads, there was a disadvantage that liquid returned to the compressor.
そこで、本発明は上記従来の欠点を解消し、負荷の大き
な範囲、冷凍装置が使用される通常の負荷範囲、さらに
、低負荷の範囲とすべての負荷範囲の負荷変動に対しで
も、冷媒回路中を流れる冷媒の量を変化させ、常に負荷
に応じて、冷凍装置に最高能力を発揮させることを可能
にしたものである。Therefore, the present invention solves the above-mentioned conventional drawbacks, and can be used in a refrigerant circuit even in a large load range, a normal load range in which refrigeration equipment is used, and even in a low load range and load fluctuations in all load ranges. By changing the amount of refrigerant flowing through the refrigeration system, it is possible to always make the refrigeration system perform at its maximum capacity depending on the load.
本発明の一実施例を第3図、第4図および第6図により
説明する。第3図に示すように、圧縮機1、凝縮器2.
絞シ装置3および蒸発器4をそれぞれ環状に連結する。An embodiment of the present invention will be described with reference to FIGS. 3, 4, and 6. As shown in FIG. 3, a compressor 1, a condenser 2.
The throttling device 3 and the evaporator 4 are each connected in a ring.
絞り装置3の途中の第一の接続位置3aには第一の冷媒
量調節容器6が連結され、第二の前記第一の接続位置3
aと蒸発器4との間に位置する第二の接続位置3bには
第二の冷媒量調節容器6が連結されている。また、吸入
管8は、圧縮機1と蒸発器4とを連結している。A first refrigerant amount adjustment container 6 is connected to a first connection position 3a in the middle of the expansion device 3, and a second connection position 3a is connected to the first connection position 3a in the middle of the expansion device 3.
A second refrigerant amount adjustment container 6 is connected to a second connection position 3b located between the refrigerant evaporator 4 and the evaporator 4. Further, the suction pipe 8 connects the compressor 1 and the evaporator 4.
また、凝縮器2と絞り装置3とを連結する接続管7には
分岐管7aが設けられ、この分岐管7aの一端は、接続
管7の途中の分岐点7bに連結され、分岐管7.aの他
端は1、前記接続管7の途中で、前記分岐点7bよりも
絞り装置3側に位置している合流点7Cに連結されてい
る。さらに、第゛4図に示すように、吸入管8と分岐管
7aとは、それぞれ第一の冷媒量調節容器6を貫通し、
さらに、第6図に示すように、前記吸入管8は第二の冷
媒量調節容器6をも貫通している。Further, a branch pipe 7a is provided in the connecting pipe 7 that connects the condenser 2 and the throttle device 3, and one end of the branch pipe 7a is connected to a branch point 7b in the middle of the connecting pipe 7. The other end of a is connected to a confluence point 7C located in the middle of the connecting pipe 7 and closer to the throttle device 3 than the branch point 7b. Furthermore, as shown in FIG. 4, the suction pipe 8 and the branch pipe 7a each penetrate the first refrigerant amount adjustment container 6,
Furthermore, as shown in FIG. 6, the suction pipe 8 also passes through the second refrigerant amount adjustment container 6.
上記した冷媒量調節装置の作用について、以下に説明す
る。The operation of the refrigerant amount adjusting device described above will be explained below.
一般に、負荷変動に対して、吸入管8の温度は敏感に、
かつ、大きく変化するが、゛第一の冷媒量調節容器6と
絞り装置3との接続位置3dの温度と、第二の冷媒量調
節容器6と絞り装置3との接続位置3bの温度とは、あ
まり変化しない。また、第一の冷媒量調節容器6と第二
の冷媒量調節容器6に蓄積される冷媒の質量は、それぞ
れ吸入管8の温度と第一の接続位置3aの温度との差と
、吸入管8の温度と第二の接続位置3bの温度との差に
関係する。さらに、第二の接続位置3bは、第一の接続
位置3aよりも、蒸発器4側にある。すなわち、第二の
接続位置3bの飽和温度は、第一の接続位置3aの飽和
温度よりも常に低いため、第一の冷媒量調節容器6も第
二の冷媒量調節容器6も同じ吸入管8と熱交換するわけ
だが、第二の冷媒量調節容器6の内部の冷媒の湿り度の
方が、第一の冷媒量調節容器5の内部の冷媒の湿り度よ
、りも常に小さくなる。Generally, the temperature of the suction pipe 8 is sensitive to load fluctuations.
Although they vary greatly, the temperature at the connection position 3d between the first refrigerant amount adjustment container 6 and the expansion device 3 and the temperature at the connection position 3b between the second refrigerant amount adjustment container 6 and the expansion device 3 are , does not change much. Further, the mass of the refrigerant accumulated in the first refrigerant amount adjustment container 6 and the second refrigerant amount adjustment container 6 is determined by the difference between the temperature of the suction pipe 8 and the temperature of the first connection position 3a, and the mass of the refrigerant accumulated in the first refrigerant amount adjustment container 6 and the second refrigerant amount adjustment container 6. 8 and the temperature at the second connection position 3b. Furthermore, the second connection position 3b is closer to the evaporator 4 than the first connection position 3a. That is, since the saturation temperature of the second connection position 3b is always lower than the saturation temperature of the first connection position 3a, both the first refrigerant amount adjustment container 6 and the second refrigerant amount adjustment container 6 are connected to the same suction pipe 8. However, the humidity of the refrigerant inside the second refrigerant amount adjustment container 6 is always smaller than the humidity of the refrigerant inside the first refrigerant amount adjustment container 5.
最高能力を発揮するように、必要冷媒が充てんされてい
るものとする。ある一定の負荷条件のもとで、冷凍装置
が運転されているとすると、吸入管8の温度もある一定
の温度に保たれる。この時、第一の冷媒量調節容器6を
貫通している吸入管8の温度は、第一の冷媒量調節容器
6と絞り装置3と連続される第一の接続位置3aの温度
よりも、負荷が大きい場合には高くな”す、通常の負荷
や低負荷の場合には低くなる。また、分岐管7aの温度
は前記第一の接続位置3aの温度よりも高い。It shall be filled with the necessary refrigerant to achieve maximum performance. Assuming that the refrigeration system is operated under a certain load condition, the temperature of the suction pipe 8 is also maintained at a certain constant temperature. At this time, the temperature of the suction pipe 8 penetrating the first refrigerant amount adjustment container 6 is higher than the temperature of the first connection position 3a where the first refrigerant amount adjustment container 6 and the expansion device 3 are connected. When the load is large, the temperature becomes high, and when the load is normal or low, the temperature becomes low.Furthermore, the temperature of the branch pipe 7a is higher than the temperature of the first connection position 3a.
このため、第一の冷媒量調節容器6の内部の冷媒の温度
は、第一の接続位置3aの冷媒の温度よりも、高負荷の
場合には高くなり、低負荷の場合には低くなる。また、
通常の負荷では、第一の冷媒量調節容器6の内部の冷媒
は、第一の接続位置3aの冷媒の温度と等しい飽和温度
を示すが、第一の冷媒量調節容器6の内部の冷媒の湿り
度と第一の接続位置3aの冷媒の湿り度は異なることに
なる。Therefore, the temperature of the refrigerant inside the first refrigerant amount adjustment container 6 becomes higher than the temperature of the refrigerant at the first connection position 3a when the load is high, and becomes lower when the load is low. Also,
Under normal load, the refrigerant inside the first refrigerant amount adjustment container 6 exhibits a saturation temperature equal to the temperature of the refrigerant at the first connection position 3a; The wetness and the wetness of the refrigerant at the first connection position 3a will be different.
また、第二の冷媒量調節容器6を貫通している吸入管8
の温度は、第二の接続位置3bの温度よりも、通常の負
荷や高負荷の場合には高くなるが、低負荷の場合には、
吸入管8は、第二の接続位置3bとほぼ同じ温度となる
。このため、第二の冷媒量調節容器6の内部の冷媒の温
度は、第二の接続位置3bの冷媒の温度よりも、通常の
負荷や高負荷の場合には、高くなる。また、低負荷では
、第二の冷媒量調節容器6の内部の冷媒は、第二の接続
位置3bの冷媒の温度と等しい飽和温度を示すが、第二
の冷媒量調節容器6の内部の冷媒の湿り度と第二の接続
位置3bの冷媒の湿り度は異なることになる。In addition, a suction pipe 8 passing through the second refrigerant amount adjustment container 6
The temperature at the second connection position 3b is higher than the temperature at the second connection position 3b when the load is normal or high, but when the load is low,
The suction pipe 8 has approximately the same temperature as the second connection position 3b. Therefore, the temperature of the refrigerant inside the second refrigerant amount adjustment container 6 becomes higher than the temperature of the refrigerant at the second connection position 3b under normal load or high load. In addition, at low load, the refrigerant inside the second refrigerant amount adjustment container 6 exhibits a saturation temperature equal to the temperature of the refrigerant at the second connection position 3b, but the refrigerant inside the second refrigerant amount adjustment container 6 The humidity of the refrigerant at the second connection position 3b is different from that of the refrigerant at the second connection position 3b.
冷媒量調節を行う際には、第一の冷媒量調節容器6と第
二の冷媒量調節容器6の内部の冷媒の湿り度の調節が重
要であシ、換言すると、冷媒の気体状態と液体状態の比
重量の差が大きいため、第一の冷媒量調節容器6と第二
の冷媒量調節容器6の内部の冷媒の液相の割合の制御が
重要である。When adjusting the amount of refrigerant, it is important to adjust the humidity of the refrigerant inside the first refrigerant amount adjustment container 6 and the second refrigerant amount adjustment container 6. In other words, the gas state and liquid state of the refrigerant Since the difference in the specific weight of the states is large, it is important to control the ratio of the liquid phase of the refrigerant inside the first refrigerant amount adjustment container 6 and the second refrigerant amount adjustment container 6.
第6図は、横軸に分岐管7aの管径をとシ、縦軸に第一
の冷媒量調節容器6の内部の冷媒の湿り度をとって、あ
る設計熱負荷条件のもとての第一の冷媒量調節容器6の
内部の冷媒の液相の割合を示したものである。例えば、
第6図において、h点で示される管径の分岐管7aを用
いたとすると、設計熱負荷条件のもとでは、第一の冷媒
量調節容器6の内部の冷媒の湿シ度はiとなる。このよ
うに、ある設計熱負荷条件のもとで、分岐管7aの管径
を適当に選択することによって、第一の冷媒量調節容器
6の内部の冷媒の湿り度を適宜選ぶことができる。In FIG. 6, the diameter of the branch pipe 7a is plotted on the horizontal axis, and the wetness of the refrigerant inside the first refrigerant amount adjustment container 6 is plotted on the vertical axis, and the result under a certain design heat load condition is shown. It shows the ratio of the liquid phase of the refrigerant inside the first refrigerant amount adjustment container 6. for example,
In FIG. 6, if a branch pipe 7a with a pipe diameter indicated by point h is used, under the design heat load conditions, the humidity of the refrigerant inside the first refrigerant amount adjustment container 6 will be i. . In this way, by appropriately selecting the pipe diameter of the branch pipe 7a under a certain design heat load condition, the wetness of the refrigerant inside the first refrigerant amount adjustment container 6 can be appropriately selected.
次に、冷凍装置が使用される通常の負荷範囲における、
冷媒量調節装置の作用について説明する。Next, in the normal load range in which the refrigeration equipment is used,
The operation of the refrigerant amount adjustment device will be explained.
今、ある負荷(例えば、設計熱負荷条件)のもとで、冷
凍装置が運転されているとする。第一の冷媒量調節容器
6の内部の冷媒の湿り度(換言すると、第一の冷媒量調
節容器6の内部に含まれる冷媒の質量)は、第6図で説
明したように、分岐管7aの管径を適当に選択すること
によって、任意に選べる。それ故、第一の冷媒量調節容
器6の内部の冷媒は、ある気液二相の飽和状態である。Assume that the refrigeration system is currently being operated under a certain load (eg, design heat load conditions). The wetness of the refrigerant inside the first refrigerant amount adjustment container 6 (in other words, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 6) is determined by the branch pipe 7a can be selected arbitrarily by appropriately selecting the pipe diameter. Therefore, the refrigerant inside the first refrigerant amount adjustment container 6 is in a certain gas-liquid two-phase saturated state.
また、通常負荷の場合、先に説明したように、第二の冷
媒量調節容器6を貫通している吸入管8の温度は、第二
の接続位置3bの温度よりもかなり高いため、第二の冷
媒量調節容器6の内部は過熱蒸気で占められる。In addition, in the case of normal load, as explained earlier, the temperature of the suction pipe 8 penetrating the second refrigerant amount adjustment container 6 is considerably higher than the temperature of the second connection position 3b. The inside of the refrigerant amount adjusting container 6 is occupied by superheated steam.
通常の負荷範囲以内で、上記の負荷よりも、負荷が増加
した場合について説明する。負荷が増加すると、この負
荷条件で冷凍装置が最高能力を発揮できる冷媒量よりも
、冷媒回路中を循環する冷媒量が不足することになるの
で、過熱度の大きい冷媒が吸入管8を通って、圧縮機1
に吸い込まれることになる。つまり、第一の冷媒量調節
容器6を貫通している吸入管8の温度は、負荷変動前よ
りも高くなる。このため、第一の冷媒量調節容器6の内
部の飽和液状態の冷媒が蒸発するので、第一の冷媒量調
節容器6の内部の冷媒の湿り度は小さくなり、冷媒の液
相の割合が小さくなる。その結果、第一の冷媒量調節容
器6の内部に含まれる冷媒の質量は、負荷変動前と比較
すると減少する。A case in which the load increases from the above load within the normal load range will be explained. When the load increases, the amount of refrigerant circulating in the refrigerant circuit becomes insufficient than the amount of refrigerant that allows the refrigeration system to exhibit its maximum capacity under this load condition. , compressor 1
will be sucked into. In other words, the temperature of the suction pipe 8 passing through the first refrigerant amount adjustment container 6 becomes higher than before the load change. Therefore, the refrigerant in the saturated liquid state inside the first refrigerant amount adjustment container 6 evaporates, so the wetness of the refrigerant inside the first refrigerant amount adjustment container 6 decreases, and the liquid phase ratio of the refrigerant decreases. becomes smaller. As a result, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 6 decreases compared to before the load change.
この減少した冷媒は、結局、絞シ装置3の途中の第一の
接続位置3aから、第一の冷媒量調節容器6の内部の冷
媒が、冷媒回路中に流れこんだ冷媒であるため、不足し
ていた冷媒回路中に冷媒が補給されることになり、吸入
管8の温度は減少し、絞り装置3の途中の第一の接続位
置3aの温度と釣合うことになる。また、第二の冷媒量
調節容器6の内部は、負荷変動前と同様、過熱蒸気で占
められるので、第二の冷媒量調節容器6に蓄積される冷
媒の質量は、はとんど変化しない。This decreased amount of refrigerant is caused by the refrigerant that has flowed into the refrigerant circuit from the first connection position 3a in the middle of the throttling device 3, so the refrigerant is insufficient. The refrigerant is replenished into the refrigerant circuit that had been in use, and the temperature of the suction pipe 8 decreases and becomes balanced with the temperature of the first connection position 3a in the middle of the expansion device 3. Furthermore, since the inside of the second refrigerant amount adjustment container 6 is occupied by superheated steam as before the load change, the mass of the refrigerant accumulated in the second refrigerant amount adjustment container 6 hardly changes. .
次に、通常の負荷範囲以内で、先に述べたある負荷(例
えば、設計熱負荷条件)よりも、負荷が減少した場合に
ついて説明する。この負荷条件で冷凍装置が最高能力を
発揮する冷媒量よりも過剰の冷媒が冷媒回路中を循環す
ることになるので、過熱度のほとんどない冷媒が、吸入
管8を通って圧縮機1に吸い込まれる。つまり、第一の
冷媒量調節容器6を貫通している吸入管8の温度は、負
荷が減少する前よりも、低くなる。このため、第一の冷
媒量調節容器6の内部の飽和蒸気状態の令息);凝縮す
るので、第一の冷媒量調節容器6の内部の冷媒の湿り度
が大きくなり、冷媒の液相の割合が大きくなる。その結
果、第一の冷媒量調節容器6の内部に含まれる冷媒の質
量は、負荷変動前と比較すると、増加する。この増加し
た冷媒は、結局、冷媒回路中の冷媒が第一の冷媒量調節
容器6に流れこんだ冷媒であるため、冷媒回路中の過剰
な冷媒が冷却されたことになり、吸入管8の温度は上昇
して第一の接続位置3aの温度と釣合う。Next, a case where the load is reduced within the normal load range from a certain load mentioned above (for example, the design thermal load condition) will be described. Under this load condition, an excess amount of refrigerant will be circulated in the refrigerant circuit than the amount at which the refrigeration system exhibits its maximum capacity, so refrigerant with almost no superheat is sucked into the compressor 1 through the suction pipe 8. It will be done. In other words, the temperature of the suction pipe 8 passing through the first refrigerant amount adjustment container 6 becomes lower than before the load decreases. For this reason, the saturated vapor state inside the first refrigerant amount adjustment container 6 condenses, so the wetness of the refrigerant inside the first refrigerant amount adjustment container 6 increases, and the proportion of the liquid phase of the refrigerant increases. becomes larger. As a result, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 6 increases compared to before the load change. This increased refrigerant is the refrigerant in the refrigerant circuit that has flowed into the first refrigerant amount adjustment container 6, so the excess refrigerant in the refrigerant circuit has been cooled, and the suction pipe 8 has been cooled down. The temperature increases to balance the temperature at the first connection location 3a.
1だ、第二の冷媒量調節容器6の内部は、負荷変動前と
同様、過熱蒸気で占められるので、その内部に蓄積され
る冷媒の質量は、はとんど変化しない。1. Since the inside of the second refrigerant amount adjustment container 6 is occupied by superheated steam as before the load change, the mass of the refrigerant accumulated inside it hardly changes.
次に、通常負荷よりも負荷がさらに高い場合(商負荷)
の冷媒量調節装置の作用について説明する。Next, if the load is even higher than the normal load (quotient load)
The operation of the refrigerant amount adjusting device will be explained.
このように負荷が高く々ると、吸入管8を通過する冷媒
の温度は、通常の負荷の場合よりも、さらに高くなるの
で、第一の冷媒量調節容器5の内容器6に含まれる冷媒
の質量は、通常負荷の場合よシも減少し、その減少した
量の冷媒が、冷媒回路中に補充されることになる。また
、第二の冷媒量調節容器6の内部は、通常負荷の場合と
同様、過熱蒸気で占められるので、その内部に蓄積され
る冷媒の質量は、はとんど変化しない。When the load is high in this way, the temperature of the refrigerant passing through the suction pipe 8 becomes higher than that under normal load, so the refrigerant contained in the inner container 6 of the first refrigerant amount adjustment container 5 The mass of the refrigerant will also be reduced under normal load, and this reduced amount of refrigerant will be replenished into the refrigerant circuit. Further, since the inside of the second refrigerant amount adjustment container 6 is occupied by superheated steam as in the case of normal load, the mass of the refrigerant accumulated therein hardly changes.
次に、通常の負荷範囲よりも、負荷がさらに低い場合(
低負荷)の冷媒量調節装置の作用について説明する。Next, if the load is even lower than the normal load range (
The operation of the refrigerant amount adjustment device (low load) will be explained.
このように、負荷が低くなると、吸入管8を通過する冷
媒の温度は、通常負荷の場合よシも、さらに低くなるの
で、第一の冷媒量調節容器6の内部は、はとんど飽和液
あるいは過冷却液で占められることになる。このため、
第一の冷媒量調節容器5に含まれる冷媒の質量は、通常
の負荷の場合よりも増加し、その増加した量の冷媒が、
冷媒回路中から除去されることになる。また、このよう
に吸入管8の温度が低くなると、吸入管8の温度と第二
の接続位置3bの温度がほぼ等しくなるので、第二の冷
媒量調節容器6の内部は、気液二相の飽和状態となる。In this way, when the load decreases, the temperature of the refrigerant passing through the suction pipe 8 becomes even lower than under normal load, so the inside of the first refrigerant amount adjustment container 6 is almost saturated. liquid or supercooled liquid. For this reason,
The mass of the refrigerant contained in the first refrigerant amount adjustment container 5 increases compared to the case of normal load, and the increased amount of refrigerant
It will be removed from the refrigerant circuit. Moreover, when the temperature of the suction pipe 8 becomes low in this way, the temperature of the suction pipe 8 and the temperature of the second connection position 3b become almost equal, so that the inside of the second refrigerant amount adjustment container 6 is in a gas-liquid two-phase state. becomes saturated.
つまり、負荷の減少にしたがって、第二の冷媒量調節容
器6の内部の冷媒の湿り度は、大きくなり、その内部に
含まれる冷媒の質量は大きくなる。That is, as the load decreases, the wetness of the refrigerant inside the second refrigerant amount adjustment container 6 increases, and the mass of the refrigerant contained therein increases.
第7図は、横軸に負荷の大きさをとり、縦軸に第一の冷
媒量調節容器5と第二の冷媒量調節容器6の内部に蓄積
〜される冷媒の質量をとって、負荷の変動に対する冷媒
量の変化を示したものである。In FIG. 7, the horizontal axis represents the magnitude of the load, and the vertical axis represents the mass of the refrigerant accumulated inside the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6. This figure shows the change in the amount of refrigerant with respect to the change in the amount of refrigerant.
第7図より明らかなように、高負荷9通常負荷の範囲で
は、主として第一の冷媒量調節容器6が冷媒量調節を行
い、低負荷の範囲では、第二の冷媒量調節容器6が冷媒
量調節を行う。As is clear from FIG. 7, in the high load 9 normal load range, the first refrigerant amount adjustment container 6 mainly adjusts the refrigerant amount, and in the low load range, the second refrigerant amount adjustment container 6 adjusts the refrigerant amount. Adjust the amount.
次に、第8図に本発明による冷媒量調節装置の他の実施
例を示す。先に説明した第3図と第8図との異なる点は
、第3図では凝縮器2と絞り装置3とを連結する接続管
7から分岐させた1分岐管7aを第一の冷媒量調節容器
′6に貫通させたことを特徴としており、第8図では前
記接続管7を分岐させずに第一の冷媒量調節゛容器6に
貫通させたことを特徴としている点である。Next, FIG. 8 shows another embodiment of the refrigerant amount adjusting device according to the present invention. The difference between FIG. 3 and FIG. 8 described above is that in FIG. In FIG. 8, the connecting pipe 7 is not branched and is passed through the first refrigerant amount adjusting container 6.
第8図で示される冷媒量調節装置も、先の実施例と同様
の作用効果が得られる。ここで、第3図と同一のものに
は同一の番号を付して、説明を省略する。The refrigerant amount adjusting device shown in FIG. 8 also provides the same effects as the previous embodiment. Here, the same parts as in FIG. 3 are given the same numbers, and the explanation will be omitted.
なお、第3召、第4図、第6図および第8図に示した例
では、凝縮器2と絞り装置3とを連結する接続管7と、
あるいは、前記接続管7がら分岐した分岐管7aと吸入
管8とを第一の冷媒量調節容器6に貫通させ、さらに、
吸入管8を第二の冷媒量調節容器6に貫通させたもので
あるが、この貫通させたことの意味は、接続管7、ある
いは分岐管7aと吸入管8とをそれぞれ第一の冷媒量調
節容器6と熱交換させること、さらに、吸入管8と第二
の冷媒量調節容器6と熱交換させることにある。故に、
接続管7、あるいは、分岐管7aと吸入管8とを第一の
冷媒量調節容器6に接触させる、また、吸入管8を第二
の冷媒量調節容器6に接触させるなどして、熱交換させ
るように配設させてもよい。In addition, in the example shown in FIG. 3, FIG. 4, FIG. 6, and FIG. 8, the connecting pipe 7 connecting the condenser 2 and the throttle device 3
Alternatively, the branch pipe 7a branched from the connecting pipe 7 and the suction pipe 8 are passed through the first refrigerant amount adjustment container 6, and further,
The suction pipe 8 is passed through the second refrigerant amount adjustment container 6, but the meaning of this penetration is that the connection pipe 7 or the branch pipe 7a and the suction pipe 8 are respectively adjusted to the first refrigerant amount. The purpose is to exchange heat with the regulating container 6 and further to exchange heat with the suction pipe 8 and the second refrigerant amount regulating container 6. Therefore,
Heat exchange is performed by bringing the connecting pipe 7 or the branch pipe 7a and the suction pipe 8 into contact with the first refrigerant amount adjustment container 6, or by bringing the suction pipe 8 into contact with the second refrigerant amount adjustment container 6. It may be arranged so as to
上述のように、本発明の冷媒量調節装置は、圧縮機、凝
縮器、絞り装置および蒸発器をそれぞれ環状に連結し、
第一の冷媒量調節容器を絞り装置の途中の第一の接続位
置に連結し、また、第二の冷媒量調節容器を前記第一の
接続位置と蒸発器との間に位置する第二の接続位置に連
結し、凝縮器と絞り装置とを連結する接続管を、または
、前記接続管から分岐した分岐管を前記第一の冷媒量調
節容器に熱交換的に配設させ、さらに、吸入管を第一の
冷媒量調節容器と第二の冷媒量調節容器とに順次熱交換
的に配設させたものである。このため、従来の冷媒量調
節装置よりも広い範囲の負荷変動に対して、冷媒量の調
節が可能である。As described above, the refrigerant amount adjusting device of the present invention includes a compressor, a condenser, a throttling device, and an evaporator connected in an annular manner,
A first refrigerant amount adjustment container is connected to a first connection position in the middle of the expansion device, and a second refrigerant amount adjustment container is connected to a second connection position located between the first connection position and the evaporator. A connecting pipe connected to the connecting position and connecting the condenser and the throttling device, or a branch pipe branched from the connecting pipe is disposed in the first refrigerant amount adjusting container in a heat exchange manner, and further, the suction The pipes are sequentially arranged in a first refrigerant amount regulating container and a second refrigerant amount regulating container for heat exchange. Therefore, the refrigerant amount can be adjusted over a wider range of load fluctuations than conventional refrigerant amount adjustment devices.
さらに、従来の冷媒量調節装置と異なり、凝縮器と絞り
装置とを連結する接続管を、あるいは、前記接続管の一
部を分岐させた分岐管を第一の冷媒量調節容器に熱交換
的に配設させているため、前記接続管の管径を、またけ
、前記分岐管の管径を適当に選ぶことにより、設計熱負
荷条件時に、第一の冷媒量調節容器に蓄積できる冷媒量
を任意り選択できる。このため、設計時に考えられる最
高負荷条件と高低負荷条件に対して、冷媒量調節機能が
十分に果たせるように、容易に第一の冷媒量調部容器の
大きさを決定できるという利点がある。Furthermore, unlike conventional refrigerant amount adjustment devices, a connecting pipe connecting a condenser and a throttling device, or a branch pipe that is a branched part of the connecting pipe, is connected to the first refrigerant amount adjusting container for heat exchange. By straddling the pipe diameter of the connecting pipe and appropriately selecting the pipe diameter of the branch pipe, the amount of refrigerant that can be accumulated in the first refrigerant amount adjustment container under the design heat load conditions can be adjusted. You can choose as you like. Therefore, there is an advantage that the size of the first refrigerant amount adjustment container can be easily determined so that the refrigerant amount adjustment function can be sufficiently performed for the maximum load condition and the high and low load conditions considered at the time of design.
又、本発明による冷媒量調節装置は、第二の冷媒量調節
容器を備えているので、特に、低負荷時の負荷変動に対
しても十分に冷媒量調節機能を果たす。このため、低負
荷時の圧縮機への液戻シーを完全に防止できる。Furthermore, since the refrigerant amount adjusting device according to the present invention is provided with the second refrigerant amount adjusting container, it can sufficiently perform the refrigerant amount adjusting function, especially in response to load fluctuations at low loads. Therefore, it is possible to completely prevent liquid from returning to the compressor at low loads.
さらに、上記説明したように、第二の冷媒量調節容器が
低負荷において、広範囲の冷媒量調節機能を果たすので
、比較的高い負荷条件において、第一の冷媒量調節容器
の冷媒量調節機能が果たせるように、分岐管の管径を選
択すれば、本発明による冷媒量調節装置は、高負荷から
低負荷までのかなり広い範囲において、冷媒量調節機能
を行う。Furthermore, as explained above, since the second refrigerant amount adjustment container performs a wide range of refrigerant amount adjustment functions under low loads, the refrigerant amount adjustment function of the first refrigerant amount adjustment container performs under relatively high load conditions. If the pipe diameter of the branch pipe is selected so that the refrigerant amount adjustment function can be achieved, the refrigerant amount adjustment device according to the present invention can perform the refrigerant amount adjustment function in a fairly wide range from high load to low load.
その結果、冷凍装置の実使用上における消費電力の節約
が大きいという長所を有する。As a result, the refrigeration system has the advantage of greatly reducing power consumption during actual use.
一部1図は従来の・冷媒量調節装置を備えた冷凍すイク
ル図、第2図は同冷媒量調節容器の熱収支を示す説明図
、第3図は本発明の一実施例における冷媒量調節装置を
備えた冷凍サイクル図、第4図は本発明に用いられる第
一の冷媒量調節容器を示す一部断面拡大図、第6図は同
第二の冷媒量調節容器を示す一部断面拡大図、第6図は
同第−の冷媒量調節容器内の冷媒の湿り度を示す説明図
、第7図は同第−および第二の冷媒量調節容器内の冷媒
の質量変化を示す説明図、第8図は本発明の他の実施例
における冷凍サイクル図である。
1・・・・・・圧縮機、2・・・・・凝縮器、3・・・
・絞り装置、4−・・・蒸発器、6 ・・ ・第一の
冷媒量調節容器、6・・・・・第二の冷媒量調節容器、
7・・・・ 接続管、8 ・・・・・吸入管、3a・・
・ ・第一の接続位置、3b ・・・・・第二の接続位
置、7a・・・・・・・分岐管。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名第工
図
第2図
第3図
第6図
JIK7図Part 1 is a diagram of a refrigeration cycle equipped with a conventional refrigerant amount adjustment device, FIG. 2 is an explanatory diagram showing the heat balance of the refrigerant amount adjustment container, and FIG. 3 is a refrigerant amount according to an embodiment of the present invention. A diagram of a refrigeration cycle equipped with an adjustment device; FIG. 4 is an enlarged partial cross-sectional view showing the first refrigerant amount adjusting container used in the present invention; FIG. 6 is a partial cross-sectional view showing the second refrigerant amount adjusting container. An enlarged view, FIG. 6 is an explanatory view showing the wetness of the refrigerant in the second refrigerant amount adjustment container, and FIG. 7 is an explanatory view showing changes in the mass of the refrigerant in the second and second refrigerant amount adjustment containers. 8 are refrigeration cycle diagrams in other embodiments of the present invention. 1... Compressor, 2... Condenser, 3...
- Squeezing device, 4 - Evaporator, 6 - First refrigerant amount adjustment container, 6... Second refrigerant amount adjustment container,
7... Connection pipe, 8... Suction pipe, 3a...
-First connection position, 3b...Second connection position, 7a...Branch pipe. Name of agent Patent attorney Toshio Nakao and one other person Construction drawings Figure 2 Figure 3 Figure 6 JIK Figure 7
Claims (1)
に連結し、前記絞り装置の途中の第一の接続位置に第一
の冷媒量調節容器を連結すると共に前記第一の接続位置
と蒸発器との間に位置する第二の接続位置に第二の冷媒
量調節容器を連結し、前記凝縮器と絞り装置とを連結す
る接続管を、または、前記接続管から分岐した分岐管を
前記第一の冷媒量調節容器に熱交換的に配設させ、さら
に、前記圧縮機と蒸発器を連結する吸入管を第一の冷媒
量調節容器と第二の冷媒量調節容器とに順次熱交換的に
配設させてなる冷凍装置における冷媒量調節装置。A compressor, a condenser, a throttling device, and an evaporator are each connected in a ring, and a first refrigerant amount adjusting container is connected to a first connecting position in the middle of the throttling device, and a first connecting position and the evaporator are connected to each other. A second refrigerant amount adjustment container is connected to a second connection position located between the connecting pipe and the connecting pipe connecting the condenser and the expansion device, or a branch pipe branched from the connecting pipe. A suction pipe connecting the compressor and the evaporator is arranged in a heat exchange manner in a first refrigerant amount adjustment container and a second refrigerant amount adjustment container in order. A refrigerant amount adjustment device in a refrigeration system installed in a refrigeration system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56143662A JPS5845450A (en) | 1981-09-10 | 1981-09-10 | Refrigerant amount adjustment device in refrigeration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56143662A JPS5845450A (en) | 1981-09-10 | 1981-09-10 | Refrigerant amount adjustment device in refrigeration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5845450A true JPS5845450A (en) | 1983-03-16 |
| JPS6240634B2 JPS6240634B2 (en) | 1987-08-28 |
Family
ID=15344007
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56143662A Granted JPS5845450A (en) | 1981-09-10 | 1981-09-10 | Refrigerant amount adjustment device in refrigeration equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5845450A (en) |
-
1981
- 1981-09-10 JP JP56143662A patent/JPS5845450A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6240634B2 (en) | 1987-08-28 |
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