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JPS6240632B2 - - Google Patents
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JPS6240632B2 - - Google Patents

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Publication number
JPS6240632B2
JPS6240632B2 JP14366081A JP14366081A JPS6240632B2 JP S6240632 B2 JPS6240632 B2 JP S6240632B2 JP 14366081 A JP14366081 A JP 14366081A JP 14366081 A JP14366081 A JP 14366081A JP S6240632 B2 JPS6240632 B2 JP S6240632B2
Authority
JP
Japan
Prior art keywords
refrigerant
refrigerant amount
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
Application number
JP14366081A
Other languages
Japanese (ja)
Other versions
JPS5845449A (en
Inventor
Masahiro Ohama
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 JP56143660A priority Critical patent/JPS5845449A/en
Publication of JPS5845449A publication Critical patent/JPS5845449A/en
Publication of JPS6240632B2 publication Critical patent/JPS6240632B2/ja
Granted legal-status Critical Current

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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とを連結する吸
入管fを冷媒量調節容器eに貫通させた構成が知
られている。
Conventionally, a refrigeration system equipped with a refrigerant amount adjustment device 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
If the suction pipe f passes through the
Since the temperature is lower than that of , a part of the refrigerant inside the refrigerant amount adjustment 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. That is, 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
負荷に対する変化と、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. In Fig. 2, the horizontal axis represents the magnitude of the load on the refrigeration system, and the vertical axis represents the amount of heat entering the refrigerant volume adjustment container e to explain the heat balance of the refrigerant volume adjustment container e with respect to load fluctuations of the refrigeration equipment. It is something. 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,
A 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 interior of the conventional refrigerant amount adjustment container e is occupied by supercooled liquid, and the refrigerant amount is adjusted only in an extremely large load range. It has the disadvantage that it does not perform the function of regulating 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, and enables refrigerant circuits to be used in large load ranges, normal load ranges in which refrigeration equipment is used, as well as low load ranges and load fluctuations in all load ranges. By changing the amount of refrigerant flowing through the system, it is possible to always make the refrigeration system perform at its maximum capacity depending on the load.

本発明の一実施例を第3図、第4図および第5
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および蒸発器4をそれ
ぞれ環状に連結する。絞り装置3の途中の第一の
接続位置3aには第一の冷媒量調節容器5が連結
され、絞り装置3の途中で前記第一の接続位置3
aよりも凝縮器2側に位置する第二の接続位置3
bには第二の冷媒量調節容器6が連結されてい
る。また、吸入管8は、圧縮機1と蒸発器4とを
連結している。また、凝縮器2と絞り装置3とを
連結する接続管7には分岐管7aが設けられ、こ
の分岐管7aの一端は、接続管7の途中の分岐点
7bに連結され、分岐管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に連結されている。
さらに、第4図に示すように、吸入管8と分岐管
7aとは、それぞれ第一の冷媒量調節容器5を貫
通し、さらに、第5図に示すように、前記吸入管
8は第二の冷媒量調節容器6をも貫通している。
An embodiment of the present invention is shown in FIGS. 3, 4 and 5.
This will be explained using figures. 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. A first refrigerant amount adjusting container 5 is connected to a first connection position 3a in the middle of the expansion device 3, and a first connection position 3a in the middle of the expansion device 3 is connected to
A second connection position 3 located closer to the condenser 2 than a
A second refrigerant amount adjustment container 6 is connected to b. Further, the suction pipe 8 connects the compressor 1 and the evaporator 4. Further, a branch pipe 7a is provided in the connecting pipe 7 that connects the condenser 2 and the throttle device 3, and one end of this branch pipe 7a is connected to a branch point 7b in the middle of the connecting pipe 7, and the branch pipe 7a is connected to a branch point 7b in the middle of the connecting pipe 7. The other end is located in the middle of the connecting pipe 7, and the throttle device 3 is located further than the branch point 7b.
It is connected to the confluence point 7c located on the side.
Furthermore, as shown in FIG. 4, the suction pipe 8 and the branch pipe 7a each penetrate the first refrigerant amount regulating container 5, and as shown in FIG. It also passes through the refrigerant amount adjustment container 6.

上記した冷媒量調節装置の作用について、以下
に説明する。
The operation of the refrigerant amount adjusting device described above will be explained below.

一般に、負荷変動に対して、吸入管8の温度は
敏感に、かつ、大きく変化するが、第一の冷媒量
調節容器5と絞り装置3との接続位置3aの温度
と、第二の冷媒量調節容器6と絞り装置3との接
続位置3bの温度とは、あまり変化しない。ま
た、第一の冷媒量調節容器5と第二の冷媒量調節
容器6に蓄積される冷媒の質量は、それぞれ吸入
管8の温度と第一の接続位置3aの温度との差
と、吸入管8の温度と第二の接続位置3bの温度
との差に関係する。さらに、第二の接続位置3b
は、第一の接続位置3aよりも、凝縮器側にあ
る。すなわち、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8と熱交換す
るわけだが、第二の冷媒量調節容器6の内部の冷
媒の湿り度の方が、第一の冷媒量調節容器5の内
部の冷媒の湿り度よりも常に大きくなる。
Generally, the temperature of the suction pipe 8 changes sensitively and greatly with respect to load fluctuations, but the temperature at the connection position 3a between the first refrigerant amount adjustment container 5 and the expansion device 3 and the second refrigerant amount change. The temperature at the connection position 3b between the regulating container 6 and the expansion device 3 does not change much. Moreover, the mass of the refrigerant accumulated in the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6 is determined by the difference between the temperature of the suction pipe 8 and the temperature of the first connection position 3a, and the mass of the refrigerant accumulated in the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6. 8 and the temperature at the second connection position 3b. Furthermore, the second connection position 3b
is located closer to the condenser than the first connection position 3a. That is, since it 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 exchange heat with the same suction pipe 8, but the second refrigerant The wetness of the refrigerant inside the amount adjusting container 6 is always greater than the wetness of the refrigerant inside the first refrigerant amount adjusting container 5.

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
8の温度もある一定の温度に保たれる。この時、
第一の冷媒量調節容器5を貫通している吸入管8
の温度は、第一の冷媒量調節容器5と絞り装置3
と連続される第一の接続位置3aの温度よりも、
負荷が大きい場合には高くなり、通常の負荷や低
負荷の場合には低くなる。また、分岐管7aの温
度は前記第一の接続位置3aの温度よりも高い。
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、第一の冷媒
量調節容器5の内部の冷媒は、第一の接続位置3
a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, 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. Assuming that the refrigeration system is operated under a certain load condition, the temperature of the suction pipe 8 is also maintained at a certain constant temperature. At this time,
Suction pipe 8 passing through the first refrigerant amount adjustment container 5
The temperature of the first refrigerant amount adjusting container 5 and the expansion device 3
than the temperature of the first connection position 3a, which is continuous with
It becomes high when the load is large, and becomes low when the load is normal or low. Further, the temperature of the branch pipe 7a is higher than the temperature of 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. Further, under normal load, the refrigerant inside the first refrigerant amount adjustment container 5 is transferred to the first connection position 3.
Although the saturation temperature is equal to the temperature of the refrigerant at point a, the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 and the refrigerant at the first connection position 3a are different.

また、第二の冷媒量調節容器6を貫通している
吸入管8の温度は、第二の接続位置3bの温度よ
りも、通常の負荷や低負荷の場合には低くなる
が、高負荷の場合には、吸入管8は、第二の接続
位置3bとほぼ同じ温度となる。このため、第二
の冷媒量調節容器6の内部の冷媒の温度は、第二
の接続位置3bとほぼ同じ温度となる。このた
め、第二の冷媒量調節容器6の内部の冷媒の温度
は、第二の接続位置3bの冷媒の温度よりも、通
常の負荷や低負荷の場合には、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 8 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 8 is at approximately the same temperature as the second connection position 3b. Therefore, the temperature of the refrigerant inside the second refrigerant amount adjustment container 6 is approximately the same temperature as the second connection position 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. Also,
At high loads, 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 has a saturation temperature. The degree of humidity and the degree of wetness of the refrigerant at the second connection position 3b will be different.

冷媒量調節を行う際には、第一の冷媒量調節容
器5と第二の冷媒量調節容器6の内部の冷媒の湿
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
の内部の冷媒の液相の割合の制御が重要である。
When adjusting the amount of refrigerant, it is important to adjust the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6. In other words, the refrigerant is in a gas state and a liquid state. Because the difference in specific weight is large, the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6
It is important to control the proportion of the liquid phase of the refrigerant inside the refrigerant.

第6図は、横軸に分岐管7a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6図において、h
点で示される管径の分岐管7aを用いたとする
と、設計熱負荷条件のもとでは、第一の冷媒量調
節容器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7
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. 6, the diameter of the branch pipe 7a is plotted on the horizontal axis, and the wetness of the refrigerant inside the first refrigerant amount adjustment container 5 is plotted on the vertical axis. This figure shows the ratio of the liquid phase of the refrigerant inside one refrigerant amount adjustment container 5. For example, in Figure 6, h
Assuming that the branch pipe 7a 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 7
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6図で説明したように、分岐
管7aの管径を適宜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。
また、通常負荷の場合、先に説明したように、第
二の冷媒量調節容器6を貫通している吸入管8の
温度は、第二の接続位置3bの温度よりも低いた
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。
Assume that the refrigeration system is currently being operated under a certain load (eg, design heat load conditions). The wetness of the refrigerant inside the first refrigerant amount adjustment container 5 (in other words, the mass of the refrigerant contained inside the first refrigerant amount adjustment container 5) is determined by can be arbitrarily selected by appropriately selecting the tube diameter. Therefore, the refrigerant inside the first refrigerant amount adjustment container 5 is in a certain gas-liquid two-phase saturated state.
In addition, in the case of normal load, as explained earlier, the temperature of the suction pipe 8 penetrating the second refrigerant amount adjustment container 6 is lower than the temperature of the second connection position 3b, so the second The interior of the refrigerant amount adjustment container 6 is occupied by supercooled liquid.

通常の負荷範囲以内で、上記の負荷よりも、負
荷が増加した場合について説明する。負荷が増加
すると、この負荷条件で冷凍装置が最高能力を発
揮できる冷媒量よりも、冷媒回路中を循環する冷
媒量が不足することになるので、過熱度の大きい
冷媒が吸入管8を通つて、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
を貫通してる吸入管8の温度は、負荷変動前より
も高くなる。
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 8 passing through becomes higher than before the load change.

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、吸入管8の温度は減少し、絞り装
置3の途中の第一の接続位置3aの温度と釣合う
ことになる。
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 eventually caused by the refrigerant flowing into the refrigerant circuit from the first connection position 3a in the middle of the expansion device 3 and the refrigerant inside the first refrigerant amount adjustment container 5. The refrigerant is replenished into the refrigerant circuit that had been in use, and the temperature of the suction pipe 8 decreases and becomes balanced with the temperature of the first connection position 3a in the middle of the expansion device 3.

また、第二の冷媒量調節容器6の内部は、負荷
変動前と同様、過冷却液で占められるので、第二
の冷媒量調節容器6に蓄積される冷媒の質量は、
ほとんど変化しない。
Furthermore, since the inside of the second refrigerant amount adjustment container 6 is occupied by supercooled liquid as before the load change, the mass of the refrigerant accumulated in the second refrigerant amount adjustment container 6 is
Almost no change.

次に、通常の負荷範囲内で、先に述べたある負
荷(例えば、設計熱負荷条件)よりも、負荷が減
少した場合について説明する。この負荷条件で冷
凍装置が最高能力を発揮する冷媒量よりも過剰の
冷媒が冷媒回路中を循環することになるので、過
熱度のほとんどない冷媒が、吸入管8を通つて圧
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8の温度は、負荷
が減少する前よりも、低くなる。このため、第一
の冷媒量調節容器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。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8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の内部は、負荷変
動前と同様、過冷却部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。
Next, a case will be described in which the load is reduced from a certain load (for example, the design thermal load condition) mentioned above within the normal load range. 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 exhibit its maximum capacity. It can be done. In other words, the temperature of the suction pipe 8 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. 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 eventually causes the refrigerant in the refrigerant circuit to reach the first refrigerant amount adjustment container 5.
Since the refrigerant has flowed into the refrigerant circuit, excess refrigerant in the refrigerant circuit has been removed, and the temperature of the suction pipe 8 rises to balance the temperature at the first connection position 3a.
Further, since the inside of the second refrigerant amount adjustment container 6 is occupied by the subcooled part liquid as before the load change, the mass of the refrigerant accumulated therein 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8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。また、第二の冷
媒量調節容器6の内部は、通常負荷の場合と同様
過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 8 becomes even lower than in the case of a 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. Further, since the inside of the second refrigerant amount adjustment container 6 is occupied by 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8を通過
する冷媒の温度は、通常の負荷の場合よりも、さ
らに高くなるので、第一の冷媒量調節容器5の内
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になる。また、このように
吸入管8の温度が高くなると、吸入管8の温度と
第二の接続位置3bの温度がほぼ等しくなるの
で、第二の冷媒量調節容器6の内部は、気液二相
の飽和状態となる。つまり、負荷の増大にしたが
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
質量は少なくなる。
When the load increases in this way, the temperature of the refrigerant passing through the suction pipe 8 becomes even 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. Moreover, when the temperature of the suction pipe 8 increases in this way, the temperature of the suction pipe 8 and the temperature of the second connection position 3b become almost equal, so that the inside of the second refrigerant amount adjustment container 6 is in a gas-liquid two-phase state. becomes saturated. 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.

第7図は、横軸に負荷の大きさをとり、縦軸に
第一の冷媒量調節容器5と第二の冷媒量調節容器
6の内部に蓄積される冷媒の質量をとつて、負荷
の変動に対する冷媒量の変化を示したものであ
る。第7図より明らかなように、低負荷、通常負
荷の範囲では、第一の冷媒量調節容器5が冷媒量
調節を行い、高負荷の範囲では、主として第二の
冷媒量調節容器6が冷媒量調節を行う。
In FIG. 7, the horizontal axis represents the magnitude of the load, and the vertical axis represents the mass of the refrigerant accumulated inside the first refrigerant amount adjustment container 5 and the second refrigerant amount adjustment container 6. This shows the change in refrigerant amount in response to fluctuations. As is clear from FIG. 7, in the low load and normal load ranges, the first refrigerant amount adjustment container 5 adjusts the refrigerant amount, and in the high load range, the second refrigerant amount adjustment container 6 mainly controls the refrigerant amount. Adjust the amount.

次に、第8図に本発明による冷媒量調節装置の
他の実施例を示す。先に説明した第3図と第8図
との異なる点は、第3図では凝縮器2と絞り装置
3とを連結する接続管7から分岐させた分岐管7
a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8図では前記接続管7a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。
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.
8 is characterized in that the connecting pipe 7a is passed through the first refrigerant amount adjusting container 5 without branching. It is a point.

第8図で示される冷媒量調節装置も、先の実施
例と同様の作用効果が得られる。ここで、第3図
と同一のものには同一の番号を付して、説明を省
略する。
The refrigerant amount adjusting device shown in FIG. 8 also provides the same effects as the previous embodiment. Here, the same parts as in FIG. 3 are given the same numbers, and the explanation will be omitted.

なお、第3図、第4図、第5図および第8図に
示した例では、凝縮器2と絞り装置3とを連結す
る接続管7と、あるいは、前記接続管7から分岐
した分岐管7aと吸入管8とを第一の冷媒量調節
容器5に貫通させ、さらに、吸入管8を第二の冷
媒量調節容器6に貫通させたものであるが、この
貫通させたことの意味は、接続管7、あるいは、
分岐管7aと吸入管8とをそれぞれ第一の冷媒量
調節容器5と熱交換させること、さらに、吸入管
8と第二の冷媒量調節容器6と熱交換させること
である。故に、接続管7、あるいは、分岐管7a
と吸入管8とを第一の冷媒量調節容器5に接触さ
せる。また、吸入管8を第二の冷媒量調節容器6
に接触させるなどして、熱交換させるように配設
させてもよい。
In the examples shown in FIGS. 3, 4, 5, and 8, 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 8 are passed through the first refrigerant amount regulating container 5, and the suction pipe 8 is further passed through the second refrigerant amount regulating container 6.The meaning of this penetration is as follows. , connecting pipe 7, or
The branch pipe 7a and the suction pipe 8 are to exchange heat with the first refrigerant amount regulating container 5, and further, the suction pipe 8 and the second refrigerant amount regulating container 6 are to exchange heat. Therefore, the connecting pipe 7 or the branch pipe 7a
and the suction pipe 8 are brought into contact with the first refrigerant amount adjustment container 5. In addition, the suction pipe 8 is connected to the second refrigerant amount adjustment container 6.
It may also be arranged so as to exchange heat, such as by bringing it into contact with.

上述のように、本発明の冷媒量調節装置は、圧
縮機、凝縮器、絞り装置および蒸発器をそれぞれ
環状に連結し、第一の冷媒量調節容器を絞り装置
の途中、あるいは、絞り装置と蒸発器との間の第
一の接続位置に連結し、また、第二の冷媒量調節
容器を絞り装置の途中で前記第一の接続位置より
も凝縮器側に位置する第二の接続位置に連結し、
凝縮器と絞り装置とを連結する接続管を、また
は、前記接続管から分岐した分岐管を前記第一の
冷媒量調節容器に熱交換的に配設させ、さらに、
吸入管を第一の冷媒量調節容器と第二の冷媒量調
節容器とに順次熱交換的に配設させたものであ
る。このため、従来の冷媒量調節装置よりも広い
範囲の負荷変動に対して、冷媒量の調節が可能で
ある。
As described above, the refrigerant amount adjusting device of the present invention connects the compressor, the condenser, the throttling device, and the evaporator in a ring, and connects the first refrigerant amount adjusting container to the middle of the throttling device or to the throttling device. A second refrigerant amount adjusting container is connected to a first connection position between the evaporator and the evaporator, and a second refrigerant amount adjusting container is connected to a second connection position located in the middle of the expansion device closer to the condenser than the first connection position. connect,
A connecting pipe connecting the condenser and the throttling device, or a branch pipe branching from the connecting pipe, is disposed in the first refrigerant amount adjusting container for heat exchange, and further,
The suction pipe is disposed in the first refrigerant amount regulating container and the second refrigerant amount regulating container in order for heat exchange. Therefore, the refrigerant amount can be adjusted over a wider range of load fluctuations than conventional refrigerant amount adjustment devices.

さらに、従来の冷媒量調節装置と異なり、凝縮
器と絞り装置とを連結する接続管を、あるいは、
前記接続管の一部を分岐させた分岐管を第一の冷
媒量調節容器に熱交換的に配設させているため、
前記接続管の管径を、または、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を決定できるという利点があ
る。
Furthermore, unlike conventional refrigerant amount adjustment devices, a connecting pipe connecting a condenser and a throttle device, or
Since a branch pipe, which is a branched part of the connecting pipe, is arranged in the first refrigerant amount adjustment container for heat exchange,
By appropriately selecting the pipe diameter of the connecting pipe or the pipe diameter of the branch pipe, under the design heat load conditions,
The amount of refrigerant that can be stored in the first refrigerant amount adjustment container can be arbitrarily selected. Therefore, there is an advantage that the size of the first refrigerant amount adjustment container can be easily determined so that the refrigerant amount adjustment function can be sufficiently performed for the maximum load condition and the minimum load condition considered at the time of design.

又、本発明による冷媒量調節装置は、第二の冷
媒量調節容器を備えているので、特に、高負荷時
の負荷変動に対しても十分に冷媒量調節機能を果
たす。さらに、低負荷時の圧縮機への液戻りを防
止できるという長所を有する。
Further, since the refrigerant amount adjusting device according to the present invention is provided with the second refrigerant amount adjusting container, the refrigerant amount adjusting function can be sufficiently performed even in response to load fluctuations particularly during high loads. Furthermore, it has the advantage of preventing liquid from returning to the compressor at low loads.

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

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図は同第一の冷
媒量調節容器内の冷媒の湿り度を示す説明図、第
7図は同第一および第二の冷媒量調節容器内の冷
媒の質量変化を示す説明図、第8図は本発明の他
の実施例における冷凍サイクル図である。 1……圧縮機、2……凝縮器、3……絞り装
置、4……蒸発器、5……第一の冷媒量調節容
器、6……第二の冷媒量調節容器、7……接続
管、8……吸入管、3a……第一の接続位置、3
b……第二の接続位置、7a……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. FIG. 4 is an enlarged partial cross-sectional view showing the first refrigerant amount adjusting container used in the present invention, FIG. 5 is an enlarged partial cross-sectional view showing the second refrigerant amount adjusting container, FIG. 6 is an explanatory diagram showing the humidity of the refrigerant in the first refrigerant amount adjustment container, FIG. 7 is an explanatory diagram showing the change in the mass of the refrigerant in the first and second refrigerant amount adjustment containers, FIG. 8 is a refrigeration cycle diagram in another embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Compressor, 2... Condenser, 3... Throttling device, 4... Evaporator, 5... First refrigerant amount adjustment container, 6... Second refrigerant amount adjustment container, 7... Connection Pipe, 8... Suction pipe, 3a... First connection position, 3
b...second connection position, 7a...branch pipe.

Claims (1)

【特許請求の範囲】[Claims] 1 圧縮機、凝縮器、絞り装置および蒸発器をそ
れぞれ環状に連結し、前記絞り装置の途中の第一
の接続位置に第一の冷媒量調節容器を連結すると
共に、前記絞り装置の途中で前記第一の接続位置
よりも凝縮器側に位置する第二の接続位置に第二
の冷媒量調節容器を連結し、前記凝縮器と絞り装
置とを連結する連続管を前記第一の冷媒量調節容
器に熱交換的に配設させ、さらに、前記圧縮機と
蒸発器とを連結する吸入管を第一の冷媒量調節容
器と第二の冷媒量調節容器とに順次熱交換的に配
設させてなる冷凍装置における冷媒量調節装置。
1. A compressor, a condenser, a throttling device, and an evaporator are each connected in a ring, and a first refrigerant amount adjustment container is connected to a first connection position in the middle of the throttling device, and the A second refrigerant amount adjustment container is connected to a second connection position located closer to the condenser than the first connection position, and a continuous pipe connecting the condenser and the expansion device is connected to the first refrigerant amount adjustment container. A suction pipe connecting the compressor and the evaporator is disposed in the container in a heat exchange manner, and a suction pipe connecting the compressor and the evaporator is sequentially disposed in the first refrigerant amount regulating container and the second refrigerant amount regulating container in a heat exchange manner. Refrigerant amount adjustment device for refrigeration equipment.
JP56143660A 1981-09-10 1981-09-10 Regulator for quantity of refrigerant in refrigerator Granted JPS5845449A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56143660A JPS5845449A (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
JP56143660A JPS5845449A (en) 1981-09-10 1981-09-10 Regulator for quantity of refrigerant in refrigerator

Publications (2)

Publication Number Publication Date
JPS5845449A JPS5845449A (en) 1983-03-16
JPS6240632B2 true JPS6240632B2 (en) 1987-08-28

Family

ID=15343958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56143660A Granted JPS5845449A (en) 1981-09-10 1981-09-10 Regulator for quantity of refrigerant in refrigerator

Country Status (1)

Country Link
JP (1) JPS5845449A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022257260A1 (en) 2021-06-07 2022-12-15 河北中化滏恒股份有限公司 Method for manufacturing 1,4-dimethylnaphthalene

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022257260A1 (en) 2021-06-07 2022-12-15 河北中化滏恒股份有限公司 Method for manufacturing 1,4-dimethylnaphthalene

Also Published As

Publication number Publication date
JPS5845449A (en) 1983-03-16

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