JPS5845451A - Refrigerant amount adjustment device in refrigeration equipment - Google Patents

Refrigerant amount adjustment device in refrigeration equipment

Info

Publication number
JPS5845451A
JPS5845451A JP56143670A JP14367081A JPS5845451A JP S5845451 A JPS5845451 A JP S5845451A JP 56143670 A JP56143670 A JP 56143670A JP 14367081 A JP14367081 A JP 14367081A JP S5845451 A JPS5845451 A JP S5845451A
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.)
Granted
Application number
JP56143670A
Other languages
Japanese (ja)
Other versions
JPS6240637B2 (en
Inventor
昌宏 尾浜
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP56143670A priority Critical patent/JPS5845451A/en
Publication of JPS5845451A publication Critical patent/JPS5845451A/en
Publication of JPS6240637B2 publication Critical patent/JPS6240637B2/ja
Granted legal-status Critical Current

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  • Devices That Are Associated With Refrigeration Equipment (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (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、絞シ装置Cと蒸発
器dとの間に連結し、さらに、圧縮機aと蒸発器di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 connecting position q in the middle of the throttling device C, or between the throttling device C and the evaporator d, and the compressor a and the evaporator di A configuration is known in which a connecting suction pipe f passes through a 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iC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、吸入管量の温
度は絞り装置Cと冷媒量゛調節容器eとの接続位tit
、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、絞り装置Cと冷媒量調
節容器eとの接続位置qの冷媒の湿9度よりも、冷媒量
調節容器eの内部の冷媒の湿υ度の方が大きくなる。つ
まシ、吸入管fの温度の万が、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θ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 throttle device iC and the refrigerant amount adjustment container e. Become saturated. However, when the suction pipe f passes through the refrigerant amount adjustment container e, the temperature of the suction pipe amount is normally determined at the connection point between the throttle device C and the refrigerant amount adjustment container e.
, q, a portion of the refrigerant inside the refrigerant amount adjustment container e condenses. Therefore, the humidity υ degree of the refrigerant inside the refrigerant amount adjustment container e is greater than the humidity 9 degrees of the refrigerant at the connection position q between the expansion device C and the refrigerant amount adjustment container e. If the temperature of the pick and suction pipe f is lower than the temperature of the connection position q, the refrigerant is simply accumulated in the refrigerant amount adjustment container θ.

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θ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とを加えた熱量になか、
この全侵入熱量は曲線q3であられしている。ここで、
曲線q5上の点I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 θ 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. Then, the total amount of heat that enters the refrigerant amount adjustment container e is the amount of heat obtained by adding ql and 92, and
This total amount of heat intrusion is represented by curve q3. here,
Point I on the curve q5 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シ小さくなる
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Iであ
られされる負荷よりも、がなり低いメいうことになる。
This is because when the load becomes considerably larger than the load at point The mass of the refrigerant accumulated inside the refrigerant amount adjustment container e does not change at all. Conversely, when the load becomes much smaller than the load at point Only the degree of supercooling 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. This means that the normal load range in which the refrigeration system is used will be much lower than the load experienced at point I.

上記説明よシ明らかなように、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、負荷が極端チ大きな範囲でし
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
縮機に液劣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 limited only in extremely large load ranges. The drawback is that the refrigerant amount adjustment function is not achieved within the normal load range in which the refrigeration system is used. Particularly when the load is low, the compressor suffers from fluid deterioration.

そこで、本発明は圧縮機と凝縮器;を連結する吐出管、
あるいは吐出管から分岐した分岐管を冷媒量調節容器に
熱交換的に配設して冷媒量調節容器に侵入する熱量を増
し、通常の負荷変動に対して鈴 も、冷媒回!中を流れる冷媒の量を変化さぞ、常□に負
荷に応して、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 provides a discharge pipe connecting a compressor and a condenser;
Alternatively, a branch pipe branched from the discharge pipe can be placed in the refrigerant amount adjustment container for heat exchange to increase the amount of heat that enters the refrigerant amount adjustment container. 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 in response to the load.

本発明の一実施例を第3図ないし第4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6は、絞シ装置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
している。また、圧縮機1と凝縮器2とを連結する吐出
管7には分岐管7aが設けられ、この分岐管7aの一端
は吐出管7の途中の分岐点7bと連結され、分岐管7a
の他端は、前記吐出管7の途中で、前記分岐点7bよシ
も凝縮器2側に位置している合流点7cと連結されてい
る。さらに、第4図に示すよ′れている。
An embodiment of the present invention will be explained with reference to FIGS. 3 and 4. FIG. As shown in FIG. 3, a compressor 1, a condenser 2, a throttle device 3, and an evaporator 4 are each connected in a ring. The refrigerant amount adjustment container 6 is connected to a connection position 3a in the middle of the throttling device 3. Further, the suction pipe 6 connects the compressor 1 and the evaporator 4. Further, a branch pipe 7a is provided in the discharge pipe 7 that connects the compressor 1 and the condenser 2, and one end of this branch pipe 7a is connected to a branch point 7b in the middle of the discharge pipe 7.
The other end is connected to a confluence point 7c located in the middle of the discharge pipe 7 on the condenser 2 side as well as the branch point 7b. Further, as shown in FIG.

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6と絞シ装置
3との接続位置3aの温度は、あまシ変化しない。
Generally, the temperature of the suction pipe 6 is sensitive to load fluctuations.
In addition, although the temperature changes greatly, the temperature at the connection position 3a between the refrigerant amount adjustment container 6 and the throttling device 3 does not change very 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6を貫通している吸
入管6の温度は、冷媒量調節容器6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、冷媒量調節容器6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6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会いため、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。第5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6の内部の冷媒の湿9度をとって、
ある設計熱負荷条件のもとての冷媒量調節容器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5
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6
の内部の冷媒の湿り度はiとなる。この冷媒量調節容器
6の内部の冷媒の湿り度は、上記説明したように、分岐
管7aの管径を適当に選択することにより、任意の湿り
度が得られるか、その他の方法として、第6図に示すよ
うに、吸入管6と分岐管7aにフィン8を設けて、その
伝熱面積金変えることによって、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。
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 penetrating the refrigerant amount adjustment container 6 is lower than the temperature at the connection position 3a between the refrigerant amount adjustment container 6 and the expansion device 3, and the temperature of the branch pipe 7a is lower than the temperature at the connection position 3a between the refrigerant amount adjustment container 6 and the expansion device 3. higher than the temperature at position 3a. Therefore, the temperature of the refrigerant inside the refrigerant amount adjustment container 5 is lower than that of the refrigerant amount adjustment container 5.
Although the saturation temperature is equal to the temperature of the refrigerant at the connection position 3a with the expansion device 3, the wetness of the refrigerant inside the refrigerant amount adjustment container 6 and the refrigerant at the connection position 3a are different. When adjusting the amount of refrigerant, it is important to adjust the wetness of the refrigerant inside the refrigerant amount adjustment container 6. In other words, since the difference in specific weight between the gas state and the liquid state of the refrigerant is large, the amount of refrigerant cannot be adjusted. Controlling the proportion of the liquid phase of the refrigerant inside the container 5 is important. In FIG. 5, the diameter of the branch pipe 7a is plotted on the horizontal axis, and the humidity of the refrigerant inside the refrigerant amount adjustment container 6 is plotted at 9 degrees on the vertical axis.
It shows the ratio of the liquid phase of the refrigerant inside the refrigerant amount adjustment container 5 under a certain design heat load condition. For example, the fifth
In the figure, if a branch pipe 7a with a pipe diameter indicated by point h is used, under the design load conditions, the refrigerant amount adjustment container 6
The wetness of the refrigerant inside is i. The wetness of the refrigerant inside the refrigerant amount adjusting container 6 can be determined by appropriately selecting the pipe diameter of the branch pipe 7a, as described above, or by using the following method. As shown in FIG. 6, by providing fins 8 on the suction pipe 6 and the branch pipe 7a and changing their heat transfer areas, the wetness of the refrigerant inside the refrigerant amount regulating container 6 can be appropriately selected.

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が、吸入管6を通って圧縮機
1に吸い込まれる。あるいは、冷媒の一部が液状のまま
吸入管6を通って圧縮機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、圧縮機1から吐
出された冷媒の温度は減少するだめ分岐管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6を貫通している吸入管6と分岐管下a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
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、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、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
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 achieve its maximum capacity under this load condition.
Refrigerant with almost no superheat is sucked into the compressor 1 through the suction pipe 6. Alternatively, part of the refrigerant will be sucked into the compressor 1 through the suction pipe 6 while remaining in liquid form,
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 discharged from the compressor 1 generally decreases, and the temperature of the branch pipe 7a also decreases. In this way, when the load decreases, both the temperature of the suction pipe 6 passing through the refrigerant amount adjustment container 6 and the lower part of the branch pipe a 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 6 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 6 increases compared to before the load change. This increased refrigerant is the refrigerant that has flowed into the refrigerant amount adjustment container 6 from the connection position 3a in the middle of the expansion device 3, so that the excess refrigerant in the refrigerant circuit has been removed. As a result, the temperature of the suction pipe 6 rises to balance the temperature of the connection position 3a.

次に負荷が増加した場合の冷媒量調節装置の作用につい
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を通って、圧縮機1に吸い込まれる
ことになる。
Next, the operation of the refrigerant amount adjusting device 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. , will be sucked into the compressor 1.

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、圧縮機1から吐出
された冷媒の温度は高くなるため、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5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。その結果、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。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。
In other words, the temperature of the suction pipe 6 becomes higher than before the load change. Furthermore, as the load increases, the temperature of the refrigerant discharged from the compressor 1 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 that pass through the refrigerant amount adjustment container 5 will 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. As a result, the mass of the refrigerant contained inside the refrigerant amount adjustment container 6 decreases compared to before the load change. This decreased refrigerant eventually flows from the connection position 3a in the middle of the expansion device 3 to the refrigerant inside the refrigerant amount adjustment container 6.
Since the refrigerant has flowed into the refrigerant circuit, the refrigerant is replenished into the refrigerant circuit that was in short supply, and the temperature of the suction pipe 6 decreases and becomes equal to the temperature of the connecting position 3a in the middle of the expansion device 3. It will balance out.

上述した冷媒量調節容器6の内部の冷媒状態の負荷に対
する変化を、第7図を用いて説明する。
The change in the state of the refrigerant inside the refrigerant amount adjusting container 6 described above with respect to the load will be explained using FIG. 7.

冷媒量調節容器6の熱収支を考える場合、従来例で説明
したように、その主な熱量は、冷媒量調節容器6の周囲
の空気からの熱伝達によって冷媒量調節容器6に侵入す
る熱量と、冷媒量調節容器5を貫通している吸入管Oに
よって冷媒量調節容器6から奪われる熱量とがある。さ
らに、本発明では、冷媒量調節容器6を貫通している分
岐管7aから冷媒量調節容器5に侵入する熱量が存在す
る。
When considering the heat balance of the refrigerant amount adjustment container 6, as explained in the conventional example, the main amount of heat is the amount of heat that enters the refrigerant amount adjustment container 6 due to heat transfer from the air around the refrigerant amount adjustment container 6. , and the amount of heat taken from the refrigerant amount adjustment container 6 by the suction pipe O penetrating the refrigerant amount adjustment container 5. Furthermore, in the present invention, there is an amount of heat that enters the refrigerant amount adjustment container 5 from the branch pipe 7a penetrating the refrigerant amount adjustment container 6.

第7図は、横軸に冷凍装装置の負荷の大きさをとり、縦
軸に冷媒量調節容器5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5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6より熱量が奪われることである。第7図
において、曲q4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q5は負荷に対する吸入管
6から侵入する熱量の変化をあられしている。さらに、
−曲線q6は、負荷に対する分岐管7aから侵入する熱
量の変化をあられしている。又、冷媒量調節容器5に侵
入する全熱量は、q4と95と96とを加えた熱量にな
り、この全侵入熱量は、曲線q7であられしている。曲
線q7上の点yは、冷媒量調節容器5への侵入熱量がな
いことをあられしている。
In FIG. 7, the horizontal axis represents the magnitude of the load on the refrigeration equipment, and the vertical axis represents the amount of heat entering the refrigerant amount adjustment container 5, and the heat balance of the refrigerant amount adjustment container 5 with respect to load fluctuations of the refrigeration equipment is calculated. This is what was explained. However, the fact that the amount of invading heat is negative means that the amount of heat is taken away from the refrigerant amount adjustment container 6. In FIG. 7, a curve q4 shows the change in the amount of heat entering from the ambient air with respect to the load, and a curve q5 shows the change in the amount of heat entering from the suction pipe 6 with respect to the load. moreover,
- The curve q6 shows the change in the amount of heat entering from the branch pipe 7a with respect to the load. Further, the total amount of heat that enters the refrigerant amount adjustment container 5 is the sum of q4, 95, and 96, and this total amount of heat that enters is represented by a curve q7. A point y on the curve q7 indicates that no amount of heat has entered the refrigerant amount adjustment container 5.

いま、第7図において、冷凍装置が使用される通常の負
荷が、点mと点nの範囲であられされるとすると、第5
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、曲線q7上の点y’に通常の負荷範囲
である点mと点nとの間に位置させることが可能となる
Now, in FIG. 7, if the normal load under which the refrigeration equipment is used is applied in the range of points m and n, then the fifth
As explained in the figure, by appropriately selecting the pipe diameter of the branch pipe 7a, it is possible to position the point y' on the curve q7 between the points m and n, which are the normal load range. Become.

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図では圧縮機1と凝縮器2とを連結する吐出管7
から分岐させた分岐管Taを冷媒量調節容器6に貫通さ
せたことを特徴としており、第8図では圧縮機1と凝縮
器2とを連結する吐出管7を分岐させずに冷媒量調節容
器6に貫通さぜ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. 3, the discharge pipe 7 connecting the compressor 1 and the condenser 2
It is characterized in that the branch pipe Ta branched from the refrigerant amount adjustment container 6 is passed through the refrigerant amount adjustment container 6, and in FIG. It is characterized by the fact that it has a 6-penetration hole.

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 their explanation will be omitted.

なお、日3図、第4図、第6図および第8図に示した例
では、圧縮機1と凝縮器2と1連結する吐出管7″′と
、あるいは、前記吐出管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6に遁 貫通させたものであるが、この貫I盲せたことの・意味
は、吐出管7、あるいは、分岐管7&と吸入管6とをそ
れぞれ冷媒量調節容器6と熱交換させることである。故
に、吐出管7、あるいは、分岐管7aと吸入管6とを冷
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 the examples shown in Figures 3, 4, 6, and 8, a discharge pipe 7'' that connects the compressor 1 and the condenser 2, or a discharge pipe branched from the discharge pipe 7 is The branch pipe 7a and the suction pipe 6 are passed through the refrigerant amount adjustment container 6, but the meaning of this blind passage is that the discharge pipe 7, or the branch pipe 7& and the suction pipe 6 Therefore, the discharge pipe 7 or the branch pipe 7a and the suction pipe 6 are arranged to be brought into contact with the refrigerant amount adjustment container 6 to exchange heat. You may have them set up.

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、蒸発益金それぞれ環状に連結し冷媒量
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、圧縮機と凝縮
器とを連結する吐出管、あるいは前記吐出管から分岐し
た分岐管と吸入管と金前明冷媒量調節容器に熱交換的に
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 has a compressor, a condenser, a throttling device, and an evaporator tube connected in a ring, and the refrigerant amount adjusting container is placed at a connecting position in the middle of the throttling device, or between the throttling device and the evaporator. A discharge pipe connected between the compressor and the condenser, or a branch pipe branched from the discharge pipe, a suction pipe, and a container for controlling the amount of refrigerant arranged for heat exchange. It is. 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、圧縮機と凝縮
器とを連結する吐出管、あるいは、前記吐出管の一部を
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、前記吐出管の管径を、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る。
Furthermore, unlike conventional refrigerant amount adjustment devices, a discharge pipe that connects the compressor and the condenser, or a branch pipe that is a branched part of the discharge pipe, is arranged in the refrigerant amount adjustment container for heat exchange. Therefore, by appropriately selecting the diameter of the discharge pipe or the 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 condition.

このため、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を決定できるという利
点がある。
Therefore, there is an advantage that the size of the 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 minimum load condition considered at the time of design.

又、本発明による冷媒量調節装置は、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
全に防止できるという長所を有する。
Furthermore, the refrigerant amount adjusting device according to the present invention has the advantage that it can completely prevent liquid from returning to the compressor, since it can sufficiently adjust the amount of refrigerant especially during low loads.

【図面の簡単な説明】[Brief explanation of drawings]

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冷媒量
調節容器を示す一部断面拡大図、第6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6図は冷媒量調
節容器の他の例を示す断面図、第7図は本発明の一実施
例における冷媒量調節容器の熱収支を示す説明図、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・・・・
・・冷媒量調節容器、6・・・・・・吸入管、7・・・
・・・吐出管、7a・・・・・・分岐管。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第 2 図 り 貢 第 3 図 第4図 第5図
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 diagram of a refrigerant amount adjustment device according to an embodiment of the present invention. FIG. 4 is an enlarged partial cross-sectional view showing the refrigerant amount adjustment container used in the present invention; FIG. 6 is an explanatory diagram showing the wetness of the refrigerant in the refrigerant amount adjustment container; FIG. 6 7 is a sectional view showing another example of the refrigerant amount adjustment container, FIG. 7 is an explanatory diagram showing the heat balance of the refrigerant amount adjustment container in one embodiment of the present invention, and FIG.
The figure is a refrigeration cycle diagram in another embodiment of the present invention. 1... Compressor, 2... Condenser, 3...
... Throttle device, 4... Evaporator, 6...
...Refrigerant amount adjustment container, 6... Suction pipe, 7...
...Discharge pipe, 7a... Branch pipe. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2 Figure 3 Figure 4 Figure 5

Claims (1)

【特許請求の範囲】[Claims] 圧縮機、凝縮器、絞り装置、蒸発器をそれぞれ環状に連
結し、前記絞シ装置の途中に、あるいは、前記絞シ装置
と蒸発器との間に冷媒量調節容器を連絡し、この冷媒量
調節容器に、前記圧縮機と凝縮器とを、連結する吐出管
、あるいは、前記吐出管から分岐した分岐管と、前記蒸
発器と圧縮機とを連結する吸入管とを熱交換的に配設し
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 refrigerant amount adjusting container is connected in the middle of the throttling device or between the throttling device and the evaporator, and the amount of refrigerant is adjusted. A discharge pipe that connects the compressor and the condenser, or a branch pipe branched from the discharge pipe, and a suction pipe that connects the evaporator and the compressor are arranged in the regulating container for heat exchange. A refrigerant amount adjustment device in a refrigeration system.
JP56143670A 1981-09-10 1981-09-10 Refrigerant amount adjustment device in refrigeration equipment Granted JPS5845451A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56143670A JPS5845451A (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
JP56143670A JPS5845451A (en) 1981-09-10 1981-09-10 Refrigerant amount adjustment device in refrigeration equipment

Publications (2)

Publication Number Publication Date
JPS5845451A true JPS5845451A (en) 1983-03-16
JPS6240637B2 JPS6240637B2 (en) 1987-08-28

Family

ID=15344201

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56143670A Granted JPS5845451A (en) 1981-09-10 1981-09-10 Refrigerant amount adjustment device in refrigeration equipment

Country Status (1)

Country Link
JP (1) JPS5845451A (en)

Also Published As

Publication number Publication date
JPS6240637B2 (en) 1987-08-28

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