JPS6242225B2 - - Google Patents
Info
- Publication number
- JPS6242225B2 JPS6242225B2 JP18500681A JP18500681A JPS6242225B2 JP S6242225 B2 JPS6242225 B2 JP S6242225B2 JP 18500681 A JP18500681 A JP 18500681A JP 18500681 A JP18500681 A JP 18500681A JP S6242225 B2 JPS6242225 B2 JP S6242225B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- amount adjustment
- refrigerant amount
- adjustment container
- load
- 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
Links
- 239000003507 refrigerant Substances 0.000 claims description 304
- 238000005057 refrigeration Methods 0.000 claims description 21
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 230000007423 decrease Effects 0.000 description 10
- 239000007788 liquid Substances 0.000 description 7
- 239000013526 supercooled liquid Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 239000007791 liquid phase Substances 0.000 description 5
- 229920006395 saturated elastomer Polymers 0.000 description 5
- 230000000149 penetrating effect Effects 0.000 description 4
- 239000012071 phase Substances 0.000 description 3
- 239000011555 saturated liquid Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
Landscapes
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
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
の冷凍能力を発揮させる冷媒量調節装置を提供す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention provides a refrigerant amount adjusting device that changes the amount of refrigerant circulating in a refrigerant circuit in response to changes in load, and exhibits the highest refrigerating capacity according to the load. be.
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b、絞り装
置c、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g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、吸入管fを冷媒量調節容器eに貫通
した構成が知られている。 Conventionally, a refrigeration system equipped with a refrigerant amount adjustment device connects a compressor a, a condenser b, a throttle device c, and an evaporator d in a ring, and throttles a refrigerant amount adjustment container e, as shown in Fig. 1. At connection position g in the middle of device c,
Alternatively, a configuration is known in which the throttle device c and the evaporator d are connected, and the suction pipe f is passed through the refrigerant amount adjustment 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gの冷媒は、気液二相
の飽和状態である。その結果、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gの冷媒と同じ飽和
状態になる。しかし、吸入管f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との接続位置
g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。これによつて、絞り
装置cと冷媒量調節容器eとの接続位置g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、このよう
に、吸入管fの温度の方が、前記接続位置g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 g between the expansion device c and the refrigerant amount adjustment container e is in a gas-liquid two-phase saturated state. As a result, 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 will be the same as that of the refrigerant at the connection position g between the expansion device c and the refrigerant amount adjustment container e. same saturation. However, when the suction pipe f passes through the refrigerant amount adjustment container e, the temperature of the suction pipe f is usually lower than the temperature at the connection position g between the throttle device c and the refrigerant amount adjustment container e, so that the refrigerant A portion of the refrigerant inside the volume control container e condenses. As a result, the wetness of the refrigerant inside the refrigerant amount adjusting container e becomes greater than the wetness of the refrigerant at the connection position g between the expansion device c and the refrigerant amount adjusting container e. That is, in this way, when the temperature of the suction pipe f is lower than the temperature of the connection position g, 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。
まず、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
からの熱伝達によつて冷媒量調節容器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によつて冷媒量調節容器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
量をとつて、冷凍装置の負荷変動に対する冷媒量
調節容器eの熱収支の状態をし示たものである。
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わし、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
をあらわしている。そして、冷媒量調節容器eに
侵入する全熱量は、前記曲線q1とq2とを加え
た熱量になり、この全侵入熱量は曲線q3であら
わしている。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。 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.
First, 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 due to heat transfer from the air surrounding the refrigerant amount adjustment container e, and the amount of heat that enters the refrigerant amount adjustment container e by the suction pipe f penetrating the refrigerant amount adjustment container e. There is an amount of heat taken away from the amount adjustment container e. Figure 2 shows the state of 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 was shown.
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 Figure 2, the curve q1 represents the change in the amount of heat entering from the surrounding air with respect to the load, and the curve q2
represents 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 the curves q1 and q2, and this total amount of heat that enters is represented by the 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であらわされる負荷
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。なぜなら、点xの負荷より
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
変動があつ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つて、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。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の内部の冷媒
は常に過冷却液状態となり、負荷変動があつて
も、冷媒量調節容器eの内部の冷媒の過冷却度が
変化するだけであつて、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であらわされる負荷よりも、かなり低
いということになる。 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 changes within a certain range around the load represented by the point x. This is because when the load is much larger than the load at point x, the refrigerant amount adjustment container e
The refrigerant inside the refrigerant is always in a superheated vapor state, and even if there is a load change, only the degree of superheating of the refrigerant inside the refrigerant amount adjustment container e changes, and the refrigerant accumulated inside the refrigerant amount adjustment container e There is almost no change in the mass of On the other hand, when the load becomes much smaller than the load at point Only the degree of cooling changes, and there is almost no change in the mass of the refrigerant accumulated inside the refrigerant amount adjustment container e. However, the typical load range in which the refrigeration system is used is the range shown by points m and n in FIG. In other words, the normal load range in which the refrigeration system is used is considerably lower than the load represented by 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、ほとんど冷媒量の調節機能を果たさず、特に
低負荷時には、圧縮機に液戻りが生じるという欠
点があつた。 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. In the normal load range in which the refrigeration system is used, it hardly functions to adjust the amount of refrigerant, and especially at low loads, it has the disadvantage that liquid returns 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ても、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,
The amount of refrigerant flowing through the refrigerant circuit is varied to accommodate large load ranges, normal load ranges in which refrigeration equipment is used, as well as low load ranges and load fluctuations across all load ranges. This makes it possible for the refrigeration equipment to demonstrate its maximum capacity accordingly.
以下、本発明をその一実施例を示す添付図面の
第3図〜第8図を参考に説明する。 Hereinafter, the present invention will be explained with reference to FIGS. 3 to 8 of the accompanying drawings showing one embodiment thereof.
第3図に示すように、冷凍サイクルは、圧縮機
1、凝縮器2、絞り装置3および蒸発器4をそれ
ぞれ環状に連結することにより構成される。そし
て第一の冷媒量調節容器5は前記絞り装置3の途
中の第一の接続位置3aに連結され、第二の冷媒
量調節容器6は前記第一の接続位置3aと凝縮器
2との間に位置する第二の接続位置3bに連結さ
れ、また、第三の冷媒量調節容器7は前記第一の
接続位置3aと蒸発器4との間に位置する第三の
接続位置3cに連結されている。また、吸入管9
は、圧縮機1と蒸発器4とを連結し、分岐管8a
の一端は、凝縮器2と絞り装置3とを連結する接
続管8の途中の分岐管8bに連結され、分岐管8
aの他端は、前記接続管8の途中で、前記分岐管
8bよりも絞り装置3側に位置している合流点8
cに連結されている。さらに、第4図に示すよう
に、吸入管9と分岐管8aとは、それぞれ第一の
冷媒量調節容器5を貫通し、さらに、第5図と第
6図に示すように、前記吸入管9は第二の冷媒量
調節容器6と第三の冷媒量調節容器7をも貫通し
ている。 As shown in FIG. 3, the refrigeration cycle is constructed by connecting a compressor 1, a condenser 2, a throttle device 3, and an evaporator 4 in a ring shape. The first refrigerant amount adjustment container 5 is connected to the first connection position 3a in the middle of the expansion device 3, and the second refrigerant amount adjustment container 6 is connected between the first connection position 3a and the condenser 2. The third refrigerant amount adjustment container 7 is connected to a third connection position 3c located between the first connection position 3a and the evaporator 4. ing. In addition, the suction pipe 9
connects the compressor 1 and evaporator 4, and connects the branch pipe 8a
One end is connected to a branch pipe 8b in the middle of a connecting pipe 8 that connects the condenser 2 and the throttle device 3.
The other end of a is located in the middle of the connecting pipe 8 and closer to the throttle device 3 than the branch pipe 8b.
connected to c. Furthermore, as shown in FIG. 4, the suction pipe 9 and the branch pipe 8a each penetrate the first refrigerant amount regulating container 5, and as shown in FIGS. 9 also passes through the second refrigerant amount adjustment container 6 and the third refrigerant amount adjustment container 7.
次に、上記冷媒量調節装置の作用について、以
下に説明する。 Next, the operation of the refrigerant amount adjusting device will be explained below.
一般に、負荷変動に対して、吸入管9の温度は
敏感に、かつ大きく変化するが、第一の接続位置
3a、第二の接続位置3bおよび第三の接続位置
3cの温度は、あまり変化しない。また、第一の
冷媒量調節容器5、第二の冷媒量調節容器6およ
び第三の冷媒量調節容器7に蓄積される冷媒の質
量は、吸入管9の温度とそれぞれ第一の接続位置
3a、第二の接続位置3bおよび第三の接続位置
3c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、凝縮
器2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
も常に高いため、第一の冷媒量調節容器5も第二
の冷媒量調節容器6も同じ吸入管9と熱交換する
わけであるが、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大きくなる。 Generally, the temperature of the suction pipe 9 changes sensitively and greatly with respect to load fluctuations, but the temperatures of the first connection position 3a, second connection position 3b, and third connection position 3c do not change much. . Moreover, the mass of the refrigerant accumulated in the first refrigerant amount adjustment container 5, the second refrigerant amount adjustment container 6, and the third refrigerant amount adjustment container 7 is determined by the temperature of the suction pipe 9 and the respective first connection position 3a. , and the temperature difference between the second connection position 3b and the third connection position 3c. Furthermore, the second connection position 3b is closer to the condenser 2 than the first connection position 3a. That is, since the saturation temperature of the second connection position 3b is always higher than the saturation temperature of the first connection position 3a, both the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6 are connected to the same suction pipe 9. However, the humidity of the refrigerant inside the second refrigerant amount adjustment container 6 is always greater than the humidity of the refrigerant inside the first refrigerant amount adjustment container 5.
また、第三の接続位置3cは、第一の接続位置
3aよりも、蒸発器4側にある。すなわち、第三
の接続位置3cの飽和温度は、第一の接続位置3
aの飽和温度よりも常に低いため、第一の冷媒量
調節容器5も第三の冷媒量調節容器7も同じ吸入
管9と熱交換するわけであるが、第三の冷媒量調
節容器7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。 Further, the third connection position 3c is closer to the evaporator 4 than the first connection position 3a. That is, the saturation temperature of the third connection position 3c is the same as that of the first connection position 3c.
Since the temperature is always lower than the saturation temperature of a, both the first refrigerant amount adjustment container 5 and the third refrigerant amount adjustment container 7 exchange heat with the same suction pipe 9. The humidity of the refrigerant inside is always smaller than the humidity of the refrigerant inside the first refrigerant amount adjustment container 5.
今、ある設計熱負荷条件に対して、冷媒装置が
最高能力を発揮するように、必要冷媒が充填され
ているものとする。そして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9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5を貫通している吸入
管9の温度は、第一の冷媒量調節容器5と絞り装
置3とが連結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り、通常の負
荷や低負荷の場合には低くなる。また、分岐管8
aの温度は前記第一の接続位置3aの温度よりも
高い。このため、第一の冷媒量調節容器5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5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。 Now, it is assumed that the refrigerant device is filled with the necessary refrigerant so that it can exhibit its maximum capacity under certain design heat load conditions. If the refrigeration system is operated under a certain load condition, the temperature of the suction pipe 9 is also maintained at a certain temperature. At this time, the temperature of the suction pipe 9 penetrating the first refrigerant amount adjustment container 5 is lower than the temperature of the first connection position 3a where the first refrigerant amount adjustment container 5 and the expansion device 3 are connected. , becomes high when the load is large, and becomes low when the load is normal or low. In addition, branch pipe 8
The temperature at point a is higher than the temperature at the first connection position 3a. Therefore, the temperature of the refrigerant inside the first refrigerant amount adjustment container 5 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. In addition, under a normal load, the saturation temperature is equal to the temperature of the refrigerant at the first connection position 3a, but the humidity of the refrigerant inside the first refrigerant amount adjustment container 5 and the refrigerant at the first connection position 3a are the same. The humidity 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9の温度は、第二の接続位置3bの温度よ
りも、通常の負荷や低負荷の場合には低くなる
が、高負荷の場合には、吸入管9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の温度の冷媒の温度よりも、通常
の負荷や低負荷の場合には、低くなる。また、高
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。 Further, the temperature of the suction pipe 9 penetrating the second refrigerant amount adjustment container 6 is lower than the temperature at the second connection position 3b under normal load or low load, but under high load. In this case, the suction pipe 9 will be at approximately the same temperature as the second connection location 3b. Therefore, the temperature of the refrigerant inside the second refrigerant amount adjustment container 6 is lower than the temperature of the refrigerant at the second connection position 3b under normal load or low load. Furthermore, under high 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.
さらに、第三の冷媒量調節容器7を貫通してい
る吸入管9の温度は、第三の接続位置3c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9は、第三の接続
位置3cとほぼ同じ温度となる。このため、第三
の冷媒量調節容器7の内部の冷媒の温度は、第三
の接続位置3c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、第三の冷媒量調節容器7の内部の冷媒は、第
三の接続位置3cの冷媒の温度と等しい飽和温度
を示すが、第三の冷媒量調節容器7の内部の冷媒
の湿り度と第三の接続位置3cの冷媒の湿り度は
異なることになる。 Furthermore, the temperature of the suction pipe 9 penetrating the third refrigerant amount adjustment container 7 is higher than the temperature at the third connection position 3c under normal load or high load, but under low load. In this case, the suction pipe 9 has approximately the same temperature as the third connection position 3c. Therefore, the temperature of the refrigerant inside the third refrigerant amount adjustment container 7 becomes higher than the temperature of the refrigerant at the third connection position 3c under normal load or high load. In addition, under low load, the refrigerant inside the third refrigerant amount adjustment container 7 exhibits a saturation temperature equal to the temperature of the refrigerant at the third connection position 3c, but the refrigerant inside the third refrigerant amount adjustment container 7 The humidity of the refrigerant at the third connection position 3c is different from that of the refrigerant at the third connection position 3c.
したがつて、冷媒量調節を行う際には、第一の
冷媒量調節容器5、第二の冷媒量調節容器6およ
び第三の冷媒量調節容器7の内部の冷媒の湿り度
の調節が重要であり、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5と第二の冷媒量調節容器6と第
三の冷媒量調節容器7の内部の冷媒の液相の割合
の制御が重要となる。 Therefore, when adjusting the amount of refrigerant, it is important to adjust the wetness of the refrigerant inside the first refrigerant amount adjustment container 5, the second refrigerant amount adjustment container 6, and the third refrigerant amount adjustment container 7. In other words, since the difference in specific weight between the gas state and the liquid state of the refrigerant is large, the inside of the first refrigerant amount adjustment container 5, the second refrigerant amount adjustment container 6, and the third refrigerant amount adjustment container 7 It is important to control the liquid phase ratio of the refrigerant.
第7図は、横軸に分岐管8aの管径をとり、縦
軸に第一の冷媒量調節容器5の内部の冷媒の湿り
度をとつて、ある設計熱負荷条件のもとでの第一
の冷媒量調節容器5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7図において、h
点で示される管径の分岐管8a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5の内部の冷媒の湿り度は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8
aの管径を適当に選択することによつて、第一の
冷媒量調節容器5の内部の冷媒の湿り度を適宜選
ぶことができる。 In FIG. 7, the diameter of the branch pipe 8a is plotted on the horizontal axis, and the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 is plotted on the vertical axis, and the temperature of the refrigerant under a certain design heat load condition is shown in FIG. This figure shows the ratio of the liquid phase of the refrigerant inside one refrigerant amount adjustment container 5. For example, in Figure 7, h
Assuming that the branch pipe 8a having the pipe diameter shown by the dot is used, the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 is i under the design heat load conditions. In this way, under certain design heat load conditions, the branch pipe 8
By appropriately selecting the pipe diameter of a, the wetness of the refrigerant inside the first refrigerant amount regulating container 5 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, the operation of the refrigerant amount adjusting device in a normal load range in which the refrigeration system is used 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仮定する。第
一の冷媒量調節容器5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5の内部に含ま
れる冷媒の質量は、第7図に示したように、分岐
管8aの管径を適当に選択することによつて、任
意に選べる。それ故、第一の冷媒量調節容器5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 now being operated under a certain load (for example, design heat load conditions). The wetness of the refrigerant inside the first refrigerant amount adjustment container 5, in other words, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 5, as shown in FIG. It can be arbitrarily selected by appropriately selecting the pipe diameter. Therefore, the refrigerant inside the first refrigerant amount adjustment container 5 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9
の温度は、第二の接続位置3bの温度よりも低い
ため、第二の冷媒量調節容器6の内部は過冷却液
で占められる。さらに、第三の冷媒量調節容器7
を貫通している吸入管9の温度は、第三の接続位
置3cよりも高いため、第三の冷媒量調節容器7
の内部は過熱蒸気で占められる。 Also, in the case of normal load, as explained earlier,
Suction pipe 9 passing through the second refrigerant amount adjustment container 6
Since the temperature at the second connection position 3b is lower than the temperature at the second connection position 3b, the inside of the second refrigerant amount adjustment container 6 is occupied by the supercooled liquid. Furthermore, a third refrigerant amount adjustment container 7
Since the temperature of the suction pipe 9 passing through the third connection position 3c is higher than that of the third connection position 3c, the third refrigerant amount adjustment container 7
The interior of 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9を通つて、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5
を貫通している吸入管9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
5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5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5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。この減少した冷媒は、結局、絞り装置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5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、これに起因して吸入管9
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。 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. , will be sucked into the compressor 1. In other words, the first refrigerant amount adjustment container 5
The temperature of the suction pipe 9 passing through becomes higher than before the load change. Therefore, the refrigerant in the saturated liquid state inside the first refrigerant amount adjustment container 5 evaporates, so the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 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 5 decreases compared to before the load change. This decreased refrigerant is the refrigerant that has flowed into the refrigerant circuit from the first connection position 3a in the middle of the expansion device 3, so the refrigerant is insufficient. The refrigerant is replenished into the refrigerant circuit, which causes the suction pipe 9 to
temperature decreases and becomes equal to the temperature at the first connection point 3a in the middle of the throttle device 3.
また、負荷変動前と同様、第二の冷媒量調節容
器6の内部は過冷却液で占められ、第三の冷媒量
調節容器7の内部は過熱蒸気で占められる。この
ため、第二の冷媒量調節容器6と第三の冷媒量調
節容器7とに蓄積される冷媒の質量は、ほとんど
変化しない。 Further, as before the load change, the inside of the second refrigerant amount adjustment container 6 is occupied by supercooled liquid, and the inside of the third refrigerant amount adjustment container 7 is occupied by superheated steam. Therefore, the mass of the refrigerant accumulated in the second refrigerant amount adjustment container 6 and the third refrigerant amount adjustment container 7 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9を通つて
圧縮機1に吸い込まれる。つまり、第一の冷媒量
調節容器5を貫通している吸入管9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5の内部の飽和蒸気状態の冷媒
が凝縮するので、第一の冷媒量調節容器5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。 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 circulating in the refrigerant circuit than the amount of refrigerant that allows the refrigeration system to achieve its maximum capacity.
Refrigerant with almost no superheat is sucked into the compressor 1 through the suction pipe 9. In other words, the temperature of the suction pipe 9 passing through the first refrigerant amount adjustment container 5 becomes lower than before the load decreases. For this reason, the refrigerant in the saturated vapor state inside the first refrigerant amount adjustment container 5 condenses, so the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 increases, and the liquid phase ratio of the refrigerant increases. growing.
その結果、第一の冷媒量調節容器5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5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除去さ
れたことになり、吸入管9の温度は上昇して第一
の接続位置3aの温度と釣合う。また、第二の冷
媒量調節容器6と第三の冷媒量調節容器7の内部
は、負荷変動前と同様、それぞれ過冷却液と過熱
蒸気で占められるので、第二の冷媒量調節容器6
と第三の冷媒量調節容器7の内部に蓄積される冷
媒の質量は、ほとんど変化しない。 As a result, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 5 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 5, so the excess refrigerant in the refrigerant circuit has been removed, and the suction pipe 9 The temperature increases to balance the temperature at the first connection location 3a. Furthermore, since the interiors of the second refrigerant amount adjustment container 6 and the third refrigerant amount adjustment container 7 are occupied by supercooled liquid and superheated steam, respectively, as before the load change, the second refrigerant amount adjustment container 6
The mass of the refrigerant accumulated inside the third refrigerant amount adjustment container 7 hardly changes.
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。 The operation of the refrigerant amount adjustment device when the load is lower than the normal load range (low load) will be explained.
このように、負荷が低くなると、吸入管9を通
過する冷媒の温度は、通常負荷の場合よりも、さ
らに低くなるので、第一の冷媒量調節容器5の内
部は、ほ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。しかし、第一の
冷媒量調節容器5が冷媒量調節を行うことが可能
な低負荷の範囲は比較的狭い部分に限られる。あ
る負荷よりも負荷が小さくなると、第一の冷媒量
調節容器5の内部の冷媒は、過冷却液状態とな
り、この負荷より負荷が減少しても、第一の冷媒
量調節容器5の内部に蓄積される冷媒の質量は、
ほとんど変化しない。これに対して、低負荷時
に、このように吸入管9の温度が低くなると、吸
入管9の温度と第三の接続装置3cの温度とがほ
ぼ等しくなるので、第三の冷媒量調節容器7の内
部は、気液二相の飽和状態となる。つまり、負荷
の減少にしたがつて、第三の冷媒量調節容器7の
内部の冷媒の温度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。しかし、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、過冷却液で占められるので、その内部に
蓄積される冷媒の質量は、ほとんど変化しない。 In this way, when the load becomes low, the temperature of the refrigerant passing through the suction pipe 9 becomes even lower than in the case of normal load, so the inside of the first refrigerant amount adjustment container 5 is almost saturated liquid or supercooled liquid. It will be occupied by liquid. Therefore, 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 is removed from the refrigerant circuit. However, the low load range in which the first refrigerant amount adjustment container 5 can adjust the amount of refrigerant is limited to a relatively narrow range. When the load becomes smaller than a certain load, the refrigerant inside the first refrigerant amount adjustment container 5 becomes a supercooled liquid state, and even if the load decreases below this load, the refrigerant inside the first refrigerant amount adjustment container 5 The mass of refrigerant accumulated is
Almost no change. On the other hand, when the temperature of the suction pipe 9 decreases in this way during low load, the temperature of the suction pipe 9 and the temperature of the third connecting device 3c become almost equal, so the third refrigerant amount adjustment container 7 The interior becomes saturated with two gas-liquid phases. That is, as the load decreases, the temperature and humidity of the refrigerant inside the third refrigerant amount adjustment container 7 increases, and the mass of the refrigerant contained therein increases. However, since the inside of the second refrigerant amount adjustment container 6 is occupied by the supercooled liquid as in the case of normal load, the mass of the refrigerant accumulated therein hardly changes.
次に、通常負荷よりも負荷がさらに高い場合
(高負荷の場合)の冷媒量調節装置の作用につい
て説明する。 Next, the operation of the refrigerant amount adjusting device when the load is higher than the normal load (high load) will be explained.
このように負荷が高くなると、吸入管9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
部は、ほとんど飽和蒸気あるいは過熱蒸気で占め
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、通常負荷の場合
よりも減少し、その減少した量の冷媒が、冷媒回
路中に補充されることなる。しかし、第一の冷媒
量調節容器5が冷媒量調節を行うことが可能な高
負荷の範囲は比較的狭い部分に限られる。ある負
荷よりも負荷が大きくなると、第一の冷媒量調節
容器5の内部の冷媒は、過熱蒸気状態となり、こ
の負荷よりも負荷が増加しても、第一の冷媒量調
節容器5の内部に蓄積される冷媒の質量は、ほと
んど変化しない。これに対して、高負荷時に、こ
のように吸入管9の温度が高くなると、吸入管9
の温度と第二の接続位置3bの温度とがほぼ等し
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。つまり、負荷の増加
にしたがつて、第二の冷媒量調節容器6の内部の
冷媒の湿り度は小さくなり、その内部に含まれる
冷媒の質量は小さくなる。しかし、第三の冷媒量
調節容器7の内部は、通常負荷の場合同様、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、通常負荷の場合とほとんど変化がな
い。 When the load increases in this way, the temperature of the refrigerant passing through the suction pipe 9 becomes higher than in the case of a normal load, so the inside of the first refrigerant amount adjustment container 5 is almost saturated steam or superheated steam. It will be occupied by Therefore, the mass of the refrigerant contained in the first refrigerant amount adjustment container 5 is reduced compared to the case of normal load, and the reduced amount of refrigerant is replenished into the refrigerant circuit. However, the high load range in which the first refrigerant amount adjustment container 5 can adjust the amount of refrigerant is limited to a relatively narrow portion. When the load becomes larger than a certain load, the refrigerant inside the first refrigerant amount adjustment container 5 becomes a superheated vapor state, and even if the load increases beyond this load, the refrigerant inside the first refrigerant amount adjustment container 5 The mass of stored refrigerant remains almost unchanged. On the other hand, when the temperature of the suction pipe 9 increases in this way under high load, the suction pipe 9
Since the temperature at the second connection position 3b is almost equal to the temperature at the second connection position 3b, the inside of the second refrigerant amount adjustment container 6 is as follows.
A state of gas-liquid two-phase saturation is reached. That is, as the load increases, the wetness of the refrigerant inside the second refrigerant amount adjustment container 6 decreases, and the mass of the refrigerant contained therein decreases. However, since the inside of the third refrigerant amount adjustment container 7 is occupied by superheated steam as in the case of normal load, the mass of the refrigerant accumulated therein is almost unchanged from that in the case of normal load.
第8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、第二の冷媒量調節容器
6および第三の冷媒量調節容器7のそれぞれの内
部に蓄積される冷媒の質量をとつて、負荷変動に
対する冷媒量の変化を示したものである。第8図
より明らかなように、高負荷の範囲では、主とし
て第二の冷媒量調節容器6が冷媒量調節を行い、
通常負荷の範囲では、主として第一の冷媒量調節
容器5が冷媒量調節を行い、低負荷の範囲では、
主として第三の冷媒量調節容器7が冷媒量調節を
行う。 In FIG. 8, the horizontal axis represents the magnitude of the load, and the vertical axis represents the accumulation inside each of the first refrigerant amount adjustment container 5, the second refrigerant amount adjustment container 6, and the third refrigerant amount adjustment container 7. The figure shows the change in the amount of refrigerant with respect to load fluctuations, based on the mass of refrigerant used. As is clear from FIG. 8, in the high load range, the second refrigerant amount adjustment container 6 mainly adjusts the refrigerant amount.
In the normal load range, the first refrigerant amount adjustment container 5 mainly adjusts the refrigerant amount, and in the low load range,
The third refrigerant amount adjustment container 7 mainly performs refrigerant amount adjustment.
次に、第9図により本発明における冷媒量調節
装置の他の実施例について説明する。 Next, another embodiment of the refrigerant amount adjusting device according to the present invention will be described with reference to FIG.
同図において、先に説明した第3図と第9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8から分岐させた分岐管8a
を第一の冷媒量調節容器5に貫通させたことを特
徴としており、第9図では前記接続管8を分岐さ
せずに第一の冷媒量調節容器5に貫通させたこと
を特徴としている点である。 In the figure, the difference between the previously explained FIG. 3 and FIG. 9 is that in FIG.
A branch pipe 8a branched from the connecting pipe 8 connecting the
It is characterized in that the connecting pipe 8 is passed through the first refrigerant amount adjusting container 5, and in FIG. 9, the connecting pipe 8 is passed through the first refrigerant amount adjusting container 5 without branching. It is.
第9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. 9 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図〜第6図および第9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
8と、あるいは、前記接続管8から分岐した分岐
管8aと吸入管9とを第一の冷媒量調節容器5に
貫通させ、さらに、吸入管9を第二の冷媒量調節
容器6と第三の冷媒量調節容器7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8、あるいは、分岐管8aと吸入管9とをそれ
ぞれ第一の冷媒量調節容器5と熱交換させるこ
と、さらに、吸入管9を第二の冷媒量調節容器6
と第三の冷媒量調節容器7とに熱交換させること
である。故に、接続管8、あるいは、分岐管8a
と吸入管9とを第一の冷媒量調節容器5に接触さ
せる。また、吸入管9を第二の冷媒量調節容器6
と第三の冷媒量調節容器7と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 the examples shown in FIGS. 3 to 6 and 9, a connecting pipe 8 connecting the condenser 2 and the throttle device 3, or a branch pipe 8a branched from the connecting pipe 8 and a suction pipe 9 is passed through the first refrigerant amount adjustment container 5, and further, the suction pipe 9 is passed through the second refrigerant amount adjustment container 6 and the third refrigerant amount adjustment container 7. This means that the connection pipe 8 or the branch pipe 8a and the suction pipe 9 are respectively allowed to exchange heat with the first refrigerant amount adjustment container 5, and that the suction pipe 9 is connected to the second refrigerant amount adjustment container 6.
and the third refrigerant amount adjustment container 7 to exchange heat. Therefore, the connecting pipe 8 or the branch pipe 8a
and the suction pipe 9 are brought into contact with the first refrigerant amount adjustment container 5. In addition, the suction pipe 9 is connected to the second refrigerant amount adjustment container 6.
The refrigerant amount adjusting container 7 may be placed in contact with the third refrigerant amount adjusting container 7 to exchange heat.
また、第3図と第9図で示した例では、第二の
接続位置3bと第三の接続位置3cとを絞り装置
3の途中に設定したが、第二の接続位置3bと第
三の接続位置3cをそれぞれ凝縮器2と絞り装置
3の間、蒸発器4と絞り装置3の間に設定しても
よい。 Furthermore, in the examples shown in FIGS. 3 and 9, the second connection position 3b and the third connection position 3c are set in the middle of the diaphragm device 3, but the second connection position 3b and the third connection position 3c are The connection position 3c may be set between the condenser 2 and the throttle device 3, and between the evaporator 4 and the throttle device 3, respectively.
さらに、第3図と第9図で示した例では、第三
の冷媒量調節容器7、第一の冷媒量調節容器5、
第二の冷媒量調節容器6の順に吸入管9を貫通さ
せたが、この順番はどのようなものであつてもよ
い。 Furthermore, in the examples shown in FIGS. 3 and 9, the third refrigerant amount adjustment container 7, the first refrigerant amount adjustment container 5,
Although the suction pipe 9 is passed through the second refrigerant amount adjustment container 6 in this order, this order may be any.
上記実施例より明らかなように、本発明の冷凍
装置における冷媒量調節装置は、圧縮機、凝縮
器、絞り装置、蒸発器および複数の冷媒量調節容
器を、連結して冷媒回路を構成し、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、第二の冷媒量調節容器を前記第一の接続位
置と凝縮器との間に位置する第二の接続位置に連
結し、また、第三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三の接続位
置に連結し、さらに前記凝縮器と絞り装置とを連
結する接続管、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
配設し、さらに前記圧縮機の吸入管を前記第一の
冷媒量調節容器、第二の冷媒量調節容器および第
三の冷媒量調節容器とそれぞれ熱交換的に配設し
たもので、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とな
り、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、または、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に選
択でき、これにより、設計時に考えられる最高負
荷条件と最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
節容器の大きさが決定でき、また、従来の冷媒量
調節装置では、比較的高い負荷の限られた範囲で
しか冷媒量調節機能を果たさなかつたが、本発明
による冷媒量調節装置は、通常負荷範囲での冷媒
量調節機能の外に、第二の冷媒量調節容器を備え
ているので、極端に負荷が高い場合にも、冷媒量
調節機能が可能であり、さらに、第三の冷媒量調
節容器を備えているので、低負荷の場合において
も冷媒量調節機能が可能であり、特に極端に負荷
が低い場合にも十分に冷媒量調節を行うため、圧
縮機への液戻りを完全に防止できる等、種々の利
点を有するものである。 As is clear from the above embodiments, the refrigerant amount adjustment device in the refrigeration system of the present invention connects a compressor, a condenser, a throttle device, an evaporator, and a plurality of refrigerant amount adjustment containers to form a refrigerant circuit, 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 condenser. a third connection position located between the first connection position and the evaporator, and a connection connecting the condenser and the throttling device; A pipe or a branch pipe branched from the connecting pipe is arranged in the first refrigerant amount regulating container for heat exchange, and the suction pipe of the compressor is connected to the first refrigerant amount regulating container and the second refrigerant amount regulating container. The refrigerant amount adjustment container and the third refrigerant amount adjustment container are each arranged for heat exchange, making it possible to adjust the refrigerant amount over a wider range of load fluctuations than with conventional refrigerant amount adjustment devices. , unlike conventional refrigerant amount adjustment devices, a connecting pipe connecting a condenser and a throttling device, or a branch pipe formed by branching a part of the connecting pipe, is arranged in the first refrigerant amount adjusting container for heat exchange. Therefore, by appropriately selecting the pipe diameter of the connecting pipe or the pipe diameter of the branch pipe, the amount of refrigerant that can be accumulated in the first refrigerant amount adjustment container can be arbitrarily selected under the design heat load conditions. As a result, 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 highest and lowest load conditions considered at the time of design. The refrigerant amount adjustment device only performs the refrigerant amount adjustment function in a limited range of relatively high loads, but the refrigerant amount adjustment device according to the present invention performs the refrigerant amount adjustment function in addition to the refrigerant amount adjustment function in the normal load range. Since it is equipped with a second refrigerant amount adjustment container, it is possible to adjust the refrigerant amount even when the load is extremely high.Furthermore, since it is equipped with a third refrigerant amount adjustment container, it can be used even when the load is extremely high. The refrigerant amount adjustment function is also possible, and since the refrigerant amount is sufficiently adjusted even when the load is extremely low, it has various advantages such as being able to completely prevent liquid from returning to the compressor.
第1図は従来の冷媒量調節装置を備えた冷凍サ
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
冷凍装置の冷媒量調節装置を備えた冷凍サイクル
図、第4図は同冷媒量調節装置における第一の冷
媒量調節容器を示す一部断面拡大図、第5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図は同第三の冷媒量調節容器を示す一部断面拡
大図、第7図は同第一の冷媒量調節容器内の冷媒
の湿り度を示す説明図、第8図は同第一の冷媒量
調節容器、第二の冷媒量調節容器および第三の冷
媒量調節容器内の冷媒の質量変化を示す説明図、
第9図は本発明の他の実施例における冷媒量調節
装置を具備した冷凍サイクル図である。
1…圧縮機、2…凝縮器、3…絞り装置、3a
…第一の接続位置、3b…第二の接続位置、3c
…第三の接続位置、4…蒸発器、5…第一の冷媒
量調節容器、6…第二の冷媒量調節容器、7…第
三の冷媒量調節容器、8…接続管、8a…分岐
管、9…吸入管。
Fig. 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 of a refrigeration system 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 adjustment container in the refrigerant amount adjustment device, and FIG. 5 is a partial sectional view showing the second refrigerant amount adjustment container. FIG. 6 is an enlarged partial cross-sectional view showing the third refrigerant amount adjustment container; FIG. 7 is an explanatory diagram showing the wetness of the refrigerant in the first refrigerant amount adjustment container; FIG. 8 is an explanatory diagram showing changes in the mass of the refrigerant in the first refrigerant amount adjustment container, the second refrigerant amount adjustment container, and the third refrigerant amount adjustment container,
FIG. 9 is a diagram of a refrigeration cycle equipped with a refrigerant amount adjusting device according to another embodiment of the present invention. 1... Compressor, 2... Condenser, 3... Squeezing device, 3a
...First connection position, 3b...Second connection position, 3c
…Third connection position, 4…Evaporator, 5…First refrigerant amount adjustment container, 6…Second refrigerant amount adjustment container, 7…Third refrigerant amount adjustment container, 8…Connection pipe, 8a…Branch Pipe, 9... Suction pipe.
Claims (1)
数の冷媒量調節容器を連結して冷媒回路を構成
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、第二の冷媒量調節容器を
前記第一の接続位置と凝縮器との間に位置する第
二の接続位置に連結し、また、第三の冷媒量調節
容器を前記第一の接続位置と蒸発器との間に位置
する第三の接続位置に連結し、さらに前記凝縮器
と絞り装置とを連結する接続管を前記第一の冷媒
量調節容器に熱交換的に配設し、さらに前記圧縮
機の吸入管を、前記第一の冷媒量調節容器、第二
の冷媒量調節容器および第三の冷媒量調節容器と
それぞれ熱交換的に配設した冷凍装置の冷媒量調
節装置。1. A compressor, a condenser, a throttle device, an evaporator, and a plurality of refrigerant amount adjustment containers are connected to form a refrigerant circuit, and a first refrigerant amount adjustment container is connected to a first connection position in the middle of the expansion device. , a second refrigerant amount adjustment container is connected to a second connection position located between the first connection position and the condenser, and a third refrigerant amount adjustment container is connected to the first connection position. A connection pipe connected to a third connection position located between the evaporator and the condenser and the expansion device is disposed in the first refrigerant amount adjustment container in a heat exchange manner, and further A refrigerant amount regulating device for a refrigeration system, wherein a suction pipe of a compressor is disposed for heat exchange with the first refrigerant amount regulating container, the second refrigerant amount regulating container, and the third refrigerant amount regulating container.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56185006A JPS5886355A (en) | 1981-11-18 | 1981-11-18 | Regulator for quantity of refrigerant of refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56185006A JPS5886355A (en) | 1981-11-18 | 1981-11-18 | Regulator for quantity of refrigerant of refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5886355A JPS5886355A (en) | 1983-05-23 |
| JPS6242225B2 true JPS6242225B2 (en) | 1987-09-07 |
Family
ID=16163122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56185006A Granted JPS5886355A (en) | 1981-11-18 | 1981-11-18 | Regulator for quantity of refrigerant of refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5886355A (en) |
-
1981
- 1981-11-18 JP JP56185006A patent/JPS5886355A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5886355A (en) | 1983-05-23 |
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