JPS6240631B2 - - Google Patents
Info
- Publication number
- JPS6240631B2 JPS6240631B2 JP10417681A JP10417681A JPS6240631B2 JP S6240631 B2 JPS6240631 B2 JP S6240631B2 JP 10417681 A JP10417681 A JP 10417681A JP 10417681 A JP10417681 A JP 10417681A JP S6240631 B2 JPS6240631 B2 JP S6240631B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- refrigerant amount
- amount adjustment
- container
- 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.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 135
- 238000005057 refrigeration Methods 0.000 claims description 13
- 230000007423 decrease Effects 0.000 description 10
- 239000007788 liquid Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 239000013526 supercooled liquid Substances 0.000 description 1
- 238000004781 supercooling Methods 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
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、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
構成であつた。 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. Connected to a connection position g in the middle of the device c or between the throttle device c and the evaporator d,
Furthermore, the suction pipe f penetrated into 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
の飽和状態であるため、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。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、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。さ
らに、熱負荷が極端に大きくない場合には、吸入
管fの温度の方が、前記接続位置gの温度よりも
低く、かつ、その両者の温度差が大きいため、冷
媒量調節容器eの内部の冷媒は過冷却液の状態と
なり、負荷変動があつても、冷媒量調節容器eの
内部の冷媒の過冷却度が変化するだけあつて、冷
媒量調節容器eの内部は、ほとんど液冷媒で占め
られることになる。つまり、従来の冷媒量調節装
置には、通常の負荷変動に対して、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。 In such a configuration, the refrigerant at the connection position g between the throttle device c and the refrigerant amount adjustment container e is in a gas-liquid two-phase saturated state, so if the suction pipe f penetrates the refrigerant amount adjustment container e, If not, the refrigerant state inside the refrigerant amount adjustment container e will be in the same saturated state as the refrigerant at the connection position g between the expansion device c and the refrigerant amount adjustment container e. 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. Therefore, the wetness of the refrigerant inside the refrigerant amount adjusting container e is greater than the wetness of the refrigerant at the connection position g between the expansion device c and the refrigerant amount adjusting container e. In other words, the temperature of the suction pipe f is
When the temperature is lower than the temperature at the connection position g, the refrigerant is simply accumulated in the refrigerant amount adjustment container e. Furthermore, when the heat load is not extremely large, the temperature of the suction pipe f is lower than the temperature of the connection position g, and the temperature difference between the two is large. The refrigerant is in a supercooled liquid state, and even if there is a load change, the degree of supercooling of the refrigerant inside the refrigerant amount adjustment container e changes, and the inside of the refrigerant amount adjustment container e is almost liquid refrigerant. It will be occupied. In other words, the conventional refrigerant amount adjusting device has the disadvantage that it hardly performs the function of adjusting the amount of refrigerant in response to normal load fluctuations, and that liquid returns to the compressor especially at low loads.
そこで、本発明は上記従来の欠点を解消し、通
常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 and changes the amount of refrigerant flowing through the refrigerant circuit even in response to normal load fluctuations, thereby making it possible for the refrigeration system to always demonstrate its maximum capacity in accordance with the load. It made it possible.
以下、本発明をその一実施例を第2図ないし第
3図により説明する。第2図に示すように、圧縮
機1、凝縮器2、絞り装置3、蒸発器4をそれぞ
れ環状に連結する。冷媒量調節容器5は、絞り装
置3の途中の接続位置3aと連結されている。ま
た、吸入管6は、圧縮機1と蒸発器4とを連結
し、分岐管7aの一端は、凝縮器2とを絞り装置
3とを連結する接続管7の途中の分岐点7bと連
結され、分岐管7aの他端は、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と連結されている。さらに、
第3図に示すように、前記吸入管6と分岐管7a
とは、それぞれ冷媒量調節容器5に熱交換的に配
設されている。 Hereinafter, one embodiment of the present invention will be explained with reference to FIGS. 2 and 3. As shown in FIG. 2, a compressor 1, a condenser 2, a throttle device 3, and an evaporator 4 are connected in a ring. The refrigerant amount adjustment container 5 is connected to a connection position 3a in the middle of the expansion device 3. Further, the suction pipe 6 connects the compressor 1 and the evaporator 4, and one end of the branch pipe 7a is connected to a branch point 7b in the middle of the connecting pipe 7 that connects the condenser 2 and the throttling device 3. The other end of the branch pipe 7a is connected to a confluence point 7c located midway along the connection pipe 7 and closer to the throttle device 3 than the branch point 7b. moreover,
As shown in FIG. 3, the suction pipe 6 and the branch pipe 7a
and are respectively disposed in the refrigerant amount regulating container 5 in a heat exchange manner.
次に、上記した冷媒量調節装置の作用について
説明する。 Next, the operation of the above-mentioned refrigerant amount adjusting device will be explained.
一般に、負荷変動に対して、吸入管6の温度は
敏感に、かつ、大きく変化するが、冷媒量調節容
器5と絞り装置3との接続位置3aの温度は、あ
まり変化しない。 Generally, the temperature of the suction pipe 6 changes sensitively and greatly with respect to load fluctuations, but the temperature of the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3 does not change much.
今、ある設計熱負荷条件に対して、冷凍装置が
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
6の温度もある一定の温度に保たれる。この時、
冷媒量調節容器5を貫通している吸入管6の温度
は、冷媒量調節容器5と絞り装置3との接続位置
3aの温度よりも低く、また、分岐管7aの温度
は前記接続位置3aの温度よりも高い。このた
め、冷媒量調節容器5の内部の冷媒の温度は、冷
媒量調節容器5と絞り装置3との接続位置3aの
冷媒の温度と等しい飽和温度を示すが、冷媒調節
容器5の内部の冷媒の湿り度と前記接続位置3a
の冷媒の湿り度は異なることになる。冷媒量調節
を行う際には、冷媒量調節容器5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、
冷媒量調節容器5の内部の冷媒の液相の割合の制
御が重要である。 Now, assume that the refrigerant is filled with the necessary refrigerant so that the refrigeration system exhibits its maximum capacity under certain design heat load conditions. When the refrigeration system is operated under a certain load condition, the temperature of the suction pipe 6 is also maintained at a certain temperature. At this time,
The temperature of the suction pipe 6 passing through the refrigerant amount adjustment container 5 is lower than the temperature at the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3, and the temperature of the branch pipe 7a is lower than the temperature at the connection position 3a. higher than the temperature. Therefore, the temperature of the refrigerant inside the refrigerant amount adjustment container 5 shows a saturation temperature equal to the temperature of the refrigerant at the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3, but the refrigerant inside the refrigerant amount adjustment container 5 humidity and the connection position 3a
The wetness of the refrigerant will be different. When adjusting the amount of refrigerant, it is important to adjust the wetness of the refrigerant inside the refrigerant amount adjustment container 5. In other words, since there is a large difference in specific weight between the gas state and the liquid state of the refrigerant,
It is important to control the ratio of the liquid phase of the refrigerant inside the refrigerant amount adjustment container 5.
第4図は、横軸に分岐管7aの管径をとり、縦
軸に冷媒量調節容器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4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、設計負荷条件
のもとでは、冷媒量調節容器の内部の冷媒の湿り
度はiとなる。この冷媒量調節容器の内部の冷媒
の湿り度は、上述の説明のように、分岐管7aの
管径を適当に選択することにより、任意の湿り度
が得られるが、その他の方法として、第5図に示
すように、吸入管6と分岐管7aにフイン8を設
けて、その伝熱面積を変えることによつても冷媒
量調節容器の内部の冷媒の湿り度を適宜選ぶこと
ができる。 In FIG. 4, the diameter of the branch pipe 7a is plotted on the horizontal axis, and the humidity of the refrigerant inside the refrigerant amount regulating container is plotted on the vertical axis, and the refrigerant amount regulating container 5 under a certain design heat load condition is shown. This shows the proportion of the liquid phase of the refrigerant inside. For example, in FIG. 4, if a branch pipe 7a having a pipe diameter indicated by point h is used, the wetness of the refrigerant inside the refrigerant amount adjustment container will be i under the design load conditions. As explained above, the humidity of the refrigerant inside the refrigerant amount adjustment container can be set to any desired humidity by appropriately selecting the pipe diameter of the branch pipe 7a. As shown in FIG. 5, the wetness of the refrigerant inside the refrigerant amount regulating container can be appropriately selected by providing fins 8 on the suction pipe 6 and the branch pipe 7a and changing the heat transfer area of the fins.
次に、負荷変動した場合の冷媒量調節装置の作
用について説明する。先ず、負荷が減少した場合
を考えると、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
い冷媒あるいは、一部液状のままの冷媒が吸入管
6を通つて圧縮機1に吸い込まれることになり、
吸入管6の温度は、負荷が減少する前よりも、低
くなる。さらに、負荷が減少すれば、一般に、凝
縮器2を通過した後の冷媒の温度は減少するた
め、分岐管7aの温度も減少する。このように、
負荷が減少すれば、冷媒量調節容器を貫通してい
る吸入管6と分岐管7aとの温度の両方共に減少
する。このため、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、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。その結果、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、絞り装置3の途中の接続位置3aから、冷
媒回路中の冷媒が冷媒量調節容器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6の温度は上昇して前
記接続位置3aの温度と釣合う。 Next, the operation of the refrigerant amount adjusting device when the load fluctuates will be explained. First, considering the case where the load decreases, an excess amount of refrigerant will be circulating in the refrigerant circuit than the amount of refrigerant that allows the refrigeration system to exhibit its maximum capacity under this load condition, so refrigerant with almost no superheat or The refrigerant, which remains partially liquid, is sucked into the compressor 1 through the suction pipe 6,
The temperature of the suction pipe 6 becomes lower than before the load is reduced. Furthermore, if the load decreases, the temperature of the refrigerant after passing through the condenser 2 generally decreases, so the temperature of the branch pipe 7a also decreases. in this way,
When the load decreases, the temperatures of both the suction pipe 6 and the branch pipe 7a passing through the refrigerant amount adjustment container decrease. Therefore, the refrigerant in a saturated vapor state inside the refrigerant amount adjustment container 5 condenses, so that the wetness of the refrigerant inside the refrigerant amount adjustment container 5 increases, and the proportion of the liquid phase of the refrigerant increases. As a result, the mass of the refrigerant contained inside the refrigerant amount adjustment container 5 increases compared to before the load change. This increased refrigerant is
After all, the refrigerant in the refrigerant circuit is the refrigerant that has flowed into the refrigerant amount adjustment container 5 from the connection position 3a in the middle of the expansion device 3, so the excess refrigerant in the refrigerant circuit has been removed, and the suction pipe The temperature at 6 increases to balance the temperature at the connection location 3a.
次に負荷が増加した場合の冷媒量調節容器の作
用について説明する。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6
を通つて、圧縮機1に吸い込まれることになる。
つまり、吸入管6の温度は、負荷変動前よりも高
くなる。また、負荷が増加すれば、一般に、凝縮
器2を通過した後の冷媒の温度も高くなるため、
分岐管7aの温度も高くなる。このように、負荷
が増加すれば、冷媒量調節容器を貫通している吸
入管6と分岐管7aとの温度が、両方共に高くな
る。このため、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、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。 Next, the action of the refrigerant amount adjustment container when the load increases 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.
It will be sucked into the compressor 1 through.
In other words, the temperature of the suction pipe 6 becomes higher than before the load change. Additionally, as the load increases, the temperature of the refrigerant after passing through the condenser 2 generally increases, so
The temperature of the branch pipe 7a also increases. In this way, if the load increases, the temperatures of both the suction pipe 6 and the branch pipe 7a, which pass through the refrigerant amount adjustment container, increase. For this reason, the refrigerant in a saturated liquid state inside the refrigerant amount adjustment container 5 evaporates, so the wetness of the refrigerant inside the refrigerant amount adjustment container 5 decreases, and the proportion of the liquid phase of the refrigerant decreases.
その結果、冷媒量調節容器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
中の接続位置3aから、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、吸入管6の温度は減少し、絞り装置
3の途中の接続位置3aの温度と釣合うことにな
る。 As a result, the mass of the refrigerant contained inside the refrigerant amount adjustment container decreases compared to before the load change. This decreased refrigerant is the refrigerant that has flowed into the refrigerant circuit from the connection position 3a in the middle of the expansion device 3, and the refrigerant inside the refrigerant amount adjustment container 5 has flowed into the refrigerant circuit, which was in short supply. As the refrigerant is replenished, the temperature of the suction pipe 6 decreases and becomes balanced with the temperature of the connecting position 3a in the middle of the expansion device 3.
次に、第6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2図と第6図
との異なる点は、第2図では凝縮器2と絞り装置
3を連結する接続管7から分岐させた分岐管7a
を冷媒量調節容器5に貫通させたことを特徴とし
ており、第6図では凝縮器2と絞り装置3を連結
する接続管7を分岐させずに冷媒量調節容器5に
貫通させたことを特徴としている点である。 Next, FIG. 6 shows another embodiment of the refrigerant amount adjusting device according to the present invention. The difference between FIG. 2 and FIG. 6 described above is that in FIG.
It is characterized by passing through the refrigerant amount adjustment container 5, and in FIG. 6, it is characterized by passing through the refrigerant amount adjustment container 5 without branching the connecting pipe 7 that connects the condenser 2 and the expansion device 3. This is the point.
第6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2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. 6 also provides the same effects as the previous embodiment. Here, the same parts as in FIG. 2 are given the same numbers, and the description thereof will be omitted.
なお、第2図、第3図、第5図および第6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から分岐
した分岐管7aと吸入管6とを冷媒量調節容器5
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6とをそれぞれ冷媒量調節容器5と熱交換さ
せることである。故に、接続管7、あるいは、分
岐管7aと吸入管6とを冷媒量調節容器5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. 2, 3, 5, and 6, a connecting pipe 7 connecting the condenser 2 and the throttle device 3, or a branch pipe branching from the connecting pipe 7 7a and the suction pipe 6 into the refrigerant amount adjustment container 5.
The purpose of this passage is to allow the connecting pipe 7 or the branch pipe 7a and the suction pipe 6 to exchange heat with the refrigerant amount adjusting container 5, respectively. Therefore, the connecting pipe 7 or the branch pipe 7a and the suction pipe 6 may be placed in contact with the refrigerant amount adjusting container 5 to exchange heat.
上述のように、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
器をそれぞれ環状に連結した冷凍装置において、
冷媒量調節容器を絞り装置の途中の接続位置に、
あるいは、絞り装置と蒸発器との間に連結し、さ
らに、凝縮器と絞り装置とを連結する接続管と、
あるいは、前記接続管から分岐した分岐管と吸入
管とを前記冷媒量調節容器に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であり、
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
管径又は、前記分岐管の管径を適当に選ぶことに
より、設計負荷条件時に、冷媒量調節容器に蓄積
できる冷媒量を任意に選択でき、これによつて、
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、容易に冷媒量調節容器の大きさが決定でき、
また特に、低負荷時の冷媒量調節も十分に行える
ため、圧縮機への液戻りを完全に防止できる等、
多大の効果を有する。 As described above, the refrigerant amount adjustment device in a refrigeration system of the present invention is a refrigeration system in which a compressor, a condenser, a throttle device, and an evaporator are each connected in a ring shape.
Place the refrigerant amount adjustment container in the connecting position in the middle of the throttling device.
Alternatively, a connecting pipe connected between the throttle device and the evaporator and further connects the condenser and the throttle device;
Alternatively, a branch pipe branched from the connecting pipe and a suction pipe are arranged in the refrigerant amount adjustment container for heat exchange, so that the refrigerant amount can be adjusted over a wider range of load fluctuations than conventional refrigerant amount adjustment devices. It is possible to adjust the
Furthermore, unlike conventional refrigerant amount adjustment devices, a connecting pipe connecting the condenser and the expansion device, or a branch pipe formed by branching a part of the connecting pipe, is arranged in the 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, it is possible to arbitrarily select the amount of refrigerant that can be stored in the refrigerant amount adjustment container under the design load conditions.
The size of the refrigerant amount adjustment container can be easily determined so that the refrigerant amount adjustment function can be adequately performed for the maximum and minimum load conditions considered at the time of design.
In addition, it is possible to fully adjust the amount of refrigerant at low loads, completely preventing liquid from returning to the compressor.
It has great effects.
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3図は
同冷媒量調節容器の一部断面拡大図、第4図は同
冷媒量調節容器内の冷媒の湿り度を示す説明図、
第5図は冷媒量調節容器の他の例を示す断面図、
第6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、3a……接続位置、4……蒸発器、5……冷
媒量調節容器、6……吸入管、7……接続管、7
a……分岐管。
FIG. 1 is a diagram of a refrigeration cycle equipped with a conventional refrigerant amount adjustment device, FIG. 2 is a diagram of a refrigeration cycle equipped with a refrigerant amount adjustment device according to an embodiment of the present invention, and FIG. 3 is a diagram of a refrigerant amount adjustment container. 4 is an explanatory diagram showing the wetness of the refrigerant in the refrigerant amount adjustment container,
FIG. 5 is a sectional view showing another example of the refrigerant amount adjustment container;
FIG. 6 is a refrigeration cycle diagram in another embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Compressor, 2... Condenser, 3... Throttle device, 3a... Connection position, 4... Evaporator, 5... Refrigerant amount adjustment container, 6... Suction pipe, 7... Connection pipe, 7
a... Branch pipe.
Claims (1)
をそれぞれ環状に連結した冷凍装置において、冷
媒量調節容器5を、前記絞り装置3と蒸発器4と
の間における絞り装置3の入口側圧力より低い圧
力となる位置に連結し、さらに、凝縮器2と絞り
装置3とを連結する接続管7と吸入管6とを、前
記冷媒量調節容器5に熱交換的に配設した冷凍装
置における冷媒量調節装置。1 Compressor 1, condenser 2, throttle device 3, evaporator 4
In the refrigeration system, the refrigerant amount adjusting container 5 is connected to a position between the expansion device 3 and the evaporator 4 where the pressure is lower than the pressure on the inlet side of the expansion device 3, and the condenser A refrigerant amount adjusting device for a refrigeration system, in which a connecting pipe 7 and a suction pipe 6 connecting the refrigerant amount adjusting container 5 and the expansion device 3 are disposed in a heat exchange manner in the refrigerant amount adjusting container 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56104176A JPS586366A (en) | 1981-07-02 | 1981-07-02 | Refrigerant amount adjustment device in refrigeration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56104176A JPS586366A (en) | 1981-07-02 | 1981-07-02 | Refrigerant amount adjustment device in refrigeration equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS586366A JPS586366A (en) | 1983-01-13 |
| JPS6240631B2 true JPS6240631B2 (en) | 1987-08-28 |
Family
ID=14373704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56104176A Granted JPS586366A (en) | 1981-07-02 | 1981-07-02 | Refrigerant amount adjustment device in refrigeration equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS586366A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60133272A (en) * | 1983-12-21 | 1985-07-16 | 三菱重工業株式会社 | Refrigerator |
-
1981
- 1981-07-02 JP JP56104176A patent/JPS586366A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS586366A (en) | 1983-01-13 |
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