JPS6240633B2 - - Google Patents
Info
- Publication number
- JPS6240633B2 JPS6240633B2 JP56143661A JP14366181A JPS6240633B2 JP S6240633 B2 JPS6240633 B2 JP S6240633B2 JP 56143661 A JP56143661 A JP 56143661A JP 14366181 A JP14366181 A JP 14366181A JP S6240633 B2 JPS6240633 B2 JP S6240633B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- amount adjustment
- refrigerant amount
- 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
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- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Sorption Type Refrigeration Machines (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に、
あるいは、絞り装置cと蒸発器dとの間に連結
し、さらに、圧縮機aと蒸発器dを連結する吸入
管fを冷媒量調節容器eに貫通させた構成が知ら
れている。 Conventionally, a refrigeration system equipped with a refrigerant amount adjustment device 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 a suction pipe f is connected between the throttle device c and the evaporator d, and further connects the compressor a and the evaporator d, 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。だから、もし、吸入管fが冷
媒量調節容器eを貫通していなければ、冷媒量調
節容器eの内部の冷媒状態は、絞り装置cと冷媒
量調節容器eとの接続位置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。 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. 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 g between the expansion device c and the refrigerant amount adjustment container e. Become saturated. However, the suction pipe f is
, the temperature of the suction pipe f is usually lower than the temperature of the connection position g between the throttle device c and the refrigerant amount adjustment container e, so that some of the refrigerant inside the refrigerant amount adjustment container e Condense. 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, 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。
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、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.
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 around the refrigerant amount adjustment container e, and the amount of heat that enters the refrigerant amount adjustment container e. There is an amount of heat taken away from the refrigerant amount adjustment container e by the suction pipe f passing through the refrigerant amount adjusting container e. Figure 2 shows the heat balance of the refrigerant amount adjustment container e with respect to load fluctuations of the refrigeration device, with the horizontal axis representing 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 represents a change in the amount of heat entering from the surrounding air with respect to the load, and a curve q2 represents a 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 q1 and q2, and this total amount of heat that enters is represented by a curve q3. Here, the point x on the curve q3 means that there is no amount of heat entering the refrigerant amount adjustment container e.
ところで、冷媒量調節容器eが冷媒量の調節機
能を果たす場合は、この点xであらわされる負荷
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
囲では、吸入管fが冷媒量調節容器eから奪う熱
量(侵入熱量が負である熱量)が大きすぎるた
め、点xで示される負荷が、冷凍装置が使用され
る通常の負荷範囲よりも、かなり高いということ
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, in the normal load range in which the refrigeration system is used, the amount of heat that the suction pipe f takes away from the refrigerant amount adjustment container e (the amount of heat for which the amount of heat entering is negative) is too large, so the load indicated by point x is is considerably higher than the normal load range in which it is used.
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ないという欠
点があつた。特に低負荷時には、圧縮機に液戻り
が生じるという短所があつた。 As is clear from the above explanation, in the normal load range in which the refrigeration system is used, the inside of the conventional refrigerant amount adjustment container e is occupied by supercooled liquid, and the refrigerant amount adjustment function is only available in extremely large load ranges. However, it has the disadvantage that it hardly functions to adjust the amount of refrigerant within the normal load range in which the refrigeration system is used. Particularly at low loads, the disadvantage was that liquid returned to the compressor.
そこで、本発明は吸入管に分岐管を設けて、冷
媒調節容器から奪う熱量を抑制し、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 provides a branch pipe in the suction pipe to suppress the amount of heat taken from the refrigerant regulating container, and changes the amount of refrigerant flowing in the refrigerant circuit even in response to normal load fluctuations, so that the amount of refrigerant flowing through the refrigerant circuit is always adjusted according to the load. This enables the refrigeration equipment to demonstrate its maximum capacity.
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、この吸入
管6に設けた分岐管6aの一端は、前記吸入管6
の途中の分岐点6bと連結され、分岐管6aの他
の端は、前記吸入管6の途中で、前記分岐点6b
よりも圧縮機1側に位置している合流点6cと連
結されている。さらに、第4図に示すように、前
記分岐管6aは、冷媒量調節容器5に熱交換的に
配設されている。 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 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 a branch pipe 6a provided in the suction pipe 6 is connected to the suction pipe 6.
The other end of the branch pipe 6a is connected to the branch point 6b in the middle of the suction pipe 6.
The confluence point 6c is located closer to the compressor 1 than the compressor 1 side. Further, as shown in FIG. 4, the branch pipe 6a is disposed in the refrigerant amount regulating container 5 for heat exchange.
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と分岐管
6a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 and the branch pipe 6a changes sensitively and greatly with respect to load fluctuations.
Connection position 3a between refrigerant amount adjustment container 5 and expansion device 3
temperature 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の温度も分岐管6a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
いる分岐管6a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の温度よりも低くな
る。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。第5図は、横軸
に分岐管6aの管径をとり、縦軸に冷媒量調節容
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6a
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5の内部の冷媒の湿り度はiとな
る。この冷媒量調節容器5の内部の冷媒の湿り度
は、上記説明したように、分岐管6a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6図に示すよう
に、分岐管6a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、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。 Now, it is assumed that the refrigerating system is filled with the necessary refrigerant so that it can exhibit 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 and the temperature of the branch pipe 6a are both maintained at a certain temperature. At this time, the temperature of the branch pipe 6a penetrating the refrigerant amount adjustment container 5 becomes lower than the temperature at the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3. 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; The humidity of the refrigerant and the humidity of the refrigerant at the connection position 3a are different. When adjusting the amount of refrigerant, use the refrigerant amount adjustment container 5.
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 the specific weight of the refrigerant between the gaseous state and the liquid state, it is important to control the proportion of the liquid phase of the refrigerant inside the refrigerant amount adjustment container 5. is important. In FIG. 5, the diameter of the branch pipe 6a is plotted on the horizontal axis, and the humidity of the refrigerant inside the refrigerant amount regulating container 5 is plotted on the vertical axis. 5 shows the ratio of the liquid phase of the refrigerant inside No. 5. For example, in FIG. 5, a branch pipe 6a with a pipe diameter indicated by point h
Assuming that, under the design load conditions, the humidity of the refrigerant inside the refrigerant amount adjustment container 5 is i. As explained above, the humidity of the refrigerant inside the refrigerant amount adjusting container 5 can be set to any desired humidity by appropriately selecting the pipe diameter of the branch pipe 6a. As shown in FIG. 6, by providing fins 8 on the branch pipe 6a and changing the heat transfer area thereof, the wetness of the refrigerant inside the refrigerant amount adjustment container 5 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と分岐管6aを通つて圧縮機
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と分岐管6aを通つて圧縮機1に
吸い込まれることになり、吸入管6と分岐管6a
の温度は、負荷が減少するよりも低くなる。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と分岐管6a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 the refrigerant with almost no superheat will be It is sucked into the compressor 1 through the suction pipe 6 and the branch pipe 6a. Alternatively, part of the refrigerant will be sucked into the compressor 1 through the suction pipe 6 and the branch pipe 6a while remaining in a liquid state, and the refrigerant will be sucked into the compressor 1 through the suction pipe 6 and the branch pipe 6a.
temperature will be lower than the load decreases. 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 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 that the excess refrigerant in the refrigerant circuit has been removed. As a result, the temperatures of the suction pipe 6 and the branch pipe 6a rise 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と
分岐管6a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と分岐管6aの温度
は、負荷変動前よりも高くなる。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
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と分岐管6a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。 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. It will be sucked into the compressor 1 through. In other words, the temperatures of the suction pipe 6 and the branch pipe 6a become higher than before the load change. 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 5 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.
The refrigerant is replenished into the refrigerant circuit that was lacking, and the temperature of the suction pipe 6 and branch pipe 6a decreases.
This balances the temperature of the connecting position 3a in the middle of the expansion device 3.
上述した冷媒量調節容器5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。冷
媒量調節容器5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5の周囲の空気からの熱伝達によつて冷媒量調
節容器5に侵入する熱量と冷媒量調節容器5を貫
通している分岐管6aによつて冷媒量調節容器5
から奪われる熱量とがある。 The change in the state of the refrigerant inside the refrigerant amount adjusting container 5 described above with respect to the load will be explained using FIG. 7. When considering the heat balance of the refrigerant amount adjustment container 5, as explained in the conventional example, the main amount of heat enters the refrigerant amount adjustment container 5 by heat transfer from the air around the refrigerant amount adjustment container 5. The refrigerant amount adjustment container 5 is controlled by the branch pipe 6a penetrating the heat amount and refrigerant amount adjustment container 5.
There is an amount of heat taken away from the body.
第7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5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
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5より熱
量が奪われることである。第7図において、曲線
q4は負荷に対する周囲空気から侵入する熱量の
変化をあらわし、曲線q5は負荷に対する分岐管
6aから侵入する熱量の変化をあらわしている。
又、冷媒量調節容器5に侵入する全熱量は、q4
とq5とを加えた熱量になり、この全侵入熱量
は、曲線q6であらわしている。曲線q6上の点
gは、冷媒量調節容器5への侵入熱量がないこと
をあらわしている。 FIG. 7 illustrates the heat balance of the refrigerant amount adjustment container 5 with respect to load fluctuations of the refrigeration device, 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 5. 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 5. In FIG. 7, a curve q4 represents a change in the amount of heat entering from the surrounding air with respect to the load, and a curve q5 represents a change in the amount of heat entering from the branch pipe 6a with respect to the load.
Also, the total amount of heat entering the refrigerant amount adjustment container 5 is q4
and q5, and this total amount of heat intrusion is represented by curve q6. A point g on the curve q6 indicates that there is no amount of heat entering 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の範囲であらわされる
とすると、第5図で説明したように、分岐管6a
の管径を適当に選択することによつて、曲線q6
上の点gを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 system is used is represented by the range between points m and n, then as explained in FIG. 5, the branch pipe 6a
By appropriately selecting the pipe diameter of the curve q6
It becomes possible to position the upper point g between points m and n, which are the normal load range.
なお、第3図、第4図および第6図に示した例
では、圧縮機1と蒸発器4とを連結する吸入管6
から分岐させた分岐管6a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、分岐管6aと冷媒量調節容器5とを熱交
換させることである。故に、分岐管6a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 addition, in the examples shown in FIGS. 3, 4, and 6, the suction pipe 6 connecting the compressor 1 and the evaporator 4 is
The branch pipe 6a branched from the refrigerant amount regulating container 5 is passed through the refrigerant amount regulating container 5, and the purpose of this passage is to allow heat exchange between the branch pipe 6a and the refrigerant amount regulating container 5. Therefore, the branch pipe 6a may be placed in contact with the refrigerant amount adjustment container 5 to exchange heat.
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、蒸発器をそれぞれ環状
に連結し、冷媒量調節容器を絞り装置の途中の接
続位置に連結し、さらに、圧縮機と蒸発器とを連
結する吸入管から分岐した分岐管を前記冷媒量調
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 connects the compressor, the condenser, the throttling device, and the evaporator in an annular manner, connects the refrigerant amount adjusting container to a connecting position in the middle of the throttling device, and further includes: A branch pipe branched from a suction pipe connecting the compressor and the evaporator is disposed in the refrigerant amount regulating container for heat exchange. Therefore, the refrigerant amount can be adjusted over a wider range of load fluctuations than conventional refrigerant amount adjustment devices.
さらに、従来の冷媒量調節装置と異なり、圧縮
機と蒸発器とを連結する吸入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。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。さらに、その冷媒量調節に際
し、電磁弁等の可動部を必要としないため、故障
の少ない、かつ信頼性の高い冷媒量調節装置とな
る。 Furthermore, unlike conventional refrigerant amount adjustment devices, a branch pipe, which is a part of the suction pipe that connects the compressor and the evaporator, is disposed in the refrigerant amount adjustment container for heat exchange. By appropriately selecting the pipe diameter of the pipe, the amount of refrigerant that can be stored in the refrigerant amount adjustment container under the design load conditions can be arbitrarily selected. For this reason,
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 minimum load condition considered at the time of design. Furthermore, since no moving parts such as electromagnetic valves are required to adjust the amount of refrigerant, the refrigerant amount adjustment device is less likely to fail and is highly reliable.
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.
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5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
である。
1……圧縮機、2……凝縮器、3……絞り装
置、4……蒸発器、5……冷媒量調節容器、6…
…吸入管、6a……分岐管。
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 diagram of a refrigerant amount adjustment device according to an embodiment of the present invention. 4 is an enlarged partial cross-sectional view showing the refrigerant amount adjustment container used in the present invention, FIG. 5 is an explanatory diagram showing the wetness of the refrigerant in the refrigerant amount adjustment container, and FIG. 6 7 is a sectional view showing another example of the refrigerant amount adjusting container, and FIG. 7 is an explanatory diagram showing the heat balance of the refrigerant amount adjusting container in one embodiment of the present invention. 1... Compressor, 2... Condenser, 3... Throttle device, 4... Evaporator, 5... Refrigerant amount adjustment container, 6...
... Suction pipe, 6a... Branch pipe.
Claims (1)
れ環状に連結し、前記絞り装置の途中に冷媒量調
節容器を連結し、この冷媒量調節容器に、前記圧
縮機と蒸発器とを連結する吸入管から分岐した分
岐管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。1. A compressor, a condenser, a throttle device, and an evaporator are each connected in a ring, a refrigerant amount adjustment container is connected in the middle of the expansion device, and the compressor and evaporator are connected to this refrigerant amount adjustment container. A refrigerant amount adjustment device in a refrigeration system, which has branch pipes branched from a suction pipe arranged for heat exchange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56143661A JPS5845453A (en) | 1981-09-10 | 1981-09-10 | Regulator for quantity of refrigerant in refrigerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56143661A JPS5845453A (en) | 1981-09-10 | 1981-09-10 | Regulator for quantity of refrigerant in refrigerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5845453A JPS5845453A (en) | 1983-03-16 |
| JPS6240633B2 true JPS6240633B2 (en) | 1987-08-28 |
Family
ID=15343981
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56143661A Granted JPS5845453A (en) | 1981-09-10 | 1981-09-10 | Regulator for quantity of refrigerant in refrigerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5845453A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0184124U (en) * | 1987-11-20 | 1989-06-05 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015078792A (en) * | 2013-10-17 | 2015-04-23 | 日立アプライアンス株式会社 | Air conditioning device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54115456A (en) * | 1978-02-28 | 1979-09-08 | Toshiba Corp | Freezing cycle |
| JPS54182451U (en) * | 1978-06-14 | 1979-12-24 |
-
1981
- 1981-09-10 JP JP56143661A patent/JPS5845453A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0184124U (en) * | 1987-11-20 | 1989-06-05 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5845453A (en) | 1983-03-16 |
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