JPS6240637B2 - - Google Patents
Info
- Publication number
- JPS6240637B2 JPS6240637B2 JP14367081A JP14367081A JPS6240637B2 JP S6240637 B2 JPS6240637 B2 JP S6240637B2 JP 14367081 A JP14367081 A JP 14367081A JP 14367081 A JP14367081 A JP 14367081A JP S6240637 B2 JPS6240637 B2 JP S6240637B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- amount adjustment
- refrigerant amount
- adjustment container
- load
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 168
- 238000005057 refrigeration Methods 0.000 claims description 18
- 230000007423 decrease Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 5
- 239000007791 liquid phase Substances 0.000 description 4
- 239000003570 air Substances 0.000 description 3
- 230000000149 penetrating effect Effects 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 239000013526 supercooled liquid Substances 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
本発明は、負荷の変化に対して、冷媒回路中を
流れる冷媒循環量を変化させ、負荷に応じて最高
冷凍能力を発揮させることができる冷媒量調節装
置の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a refrigerant amount adjusting device that can change the amount of refrigerant circulating in a refrigerant circuit in response to a change in load, and can exhibit the maximum refrigerating capacity according to the load. It is something.
従来、冷媒量調節装置を備えた冷凍装置は、第
1図に示すように、圧縮機a、凝縮器b、絞り装
置c、蒸発器dをそれぞれ環状に連結し、冷媒量
調節容器eを絞り装置cの途中の接続位置g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
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. 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, the curve q 1 represents the change in the amount of heat entering from the surrounding air with respect to the load, and the curve q 2 represents the change in the amount of heat entering from the suction pipe f with respect to the load. The total amount of heat that enters the refrigerant amount adjustment container e is the sum of q 1 and q 2 , and this total amount of heat that enters is represented by the curve q 3 . Here, the point x on the curve q3 means that there is no amount of heat entering the refrigerant amount adjustment container e.
ところで、冷媒量調節容器eが冷媒量の調節機
能を果たす場合は、この点xであらわされる負荷
をほぼ中心として、その前後のある範囲の負荷変
動の場合だけである。なぜなら、点xの負荷より
も負荷がかなり大きくなると、冷媒量調節容器e
の内部の冷媒は常に過熱蒸気の状態となり、負荷
変動があつても冷媒量調節容器eの内部の冷媒の
過熱度が変化するだけであつて、冷媒量調節容器
eの内部に蓄積される冷媒の質量には、ほとんど
変化がない。逆に、点xの負荷よりも負荷がかな
り小さくなると、冷媒量調節容器eの内部の冷媒
は常に過冷却液状態となり、負荷変動があつて
も、冷媒量調節容器eの内部の冷媒の過冷却度が
変化するだけであつて、冷媒量調節容器eの内部
に蓄積される冷媒の質量にはほとんど変化がな
い。しかし、冷凍装置が使用される通常の負荷の
範囲は、第2図の点mと点nで示される範囲であ
る。つまり、冷凍装置が使用される通常の負荷範
囲は、点xであらわされる負荷よりも、かなり低
いということになる。 By the way, the case where the refrigerant amount adjustment container e performs the refrigerant amount adjustment function is only when the load changes within a certain range around the load represented by the point x. This is because when the load becomes much larger than the load at point x, the refrigerant amount adjustment container e
The refrigerant inside 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
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 discharge pipe connecting the compressor and the condenser, or a branch pipe branched from the discharge pipe, to the refrigerant amount adjustment container for heat exchange to increase the amount of heat that enters the refrigerant amount adjustment container. This system changes the amount of refrigerant flowing through the refrigerant circuit even when the load fluctuates, allowing the refrigeration system to always perform at its maximum capacity in accordance with 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、圧縮器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
岐管7bよりも凝縮器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
うに、前記吸入管6と分岐管7aとは、それぞれ
冷媒量調節容器5に貫通させて熱交換的に配設さ
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. 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 end is connected to a confluence point 7c located in the middle of the discharge pipe 7 closer to the condenser 2 than the branch pipe 7b. Further, as shown in FIG. 4, the suction pipe 6 and the branch pipe 7a are respectively disposed through 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の温度は
敏感に、かつ、大きく変化するが、冷媒量調節容
器5と絞り装置3との接続位置3aの温度は、あ
まり変化しない。 Generally, the temperature of the suction pipe 6 changes sensitively and greatly with respect to load fluctuations, but the temperature of the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3 does not change much.
今、ある設計熱負荷条件に対して、冷凍装置が
最高能力を発揮するように、必要冷媒が充てんさ
れているものとする。ある一定の負荷条件のもと
で、冷凍装置が運転されているとすると、吸入管
6の温度もある一定の温度に保たれる。この時、
冷媒量調節容器5を貫通している吸入管6の温度
は、冷媒量調節容器5と絞り装置3との接続位置
3aの温度よりも低く、また、分岐管7aの温度
は前記接続位置3aの温度よりも高い。このた
め、冷媒量調節容器5の内部の冷媒の温度は、冷
媒量調節容器5と絞り装置3との接続位置3aの
冷媒の温度と等しい飽和温度を示すが、冷媒量調
節容器5の内部の冷媒の湿り度と前記接続位置3
a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7
a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7aの管径を適当に選択する
ことにより、任意の湿り度が得られるが、その他
の方法として、第6図に示すように、吸入管6と
分岐管7aにフイン8を設けて、その伝熱面積を
変えることによつて、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, 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 5 is lower than the temperature of the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3, and the temperature of the branch pipe 7a is lower than the temperature of the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3. higher than the temperature. Therefore, the temperature of the refrigerant inside the refrigerant amount adjustment container 5 shows a saturation temperature equal to the temperature of the refrigerant at the connection position 3a between the refrigerant amount adjustment container 5 and the expansion device 3; Wetness of refrigerant and connection position 3
The wetness of the refrigerant in a will be different. When adjusting the amount of refrigerant, it is important to adjust the wetness of the refrigerant inside the refrigerant amount adjustment container 5. In other words, since there is a large difference in specific weight between the gas state and the liquid state of the refrigerant, it is important to adjust the amount of refrigerant. Controlling the proportion of the liquid phase of the refrigerant inside the container 5 is important. Figure 5 shows branch pipe 7 on the horizontal axis.
The liquid phase ratio of the refrigerant inside the refrigerant amount adjustment container 5 under a certain design heat load condition is calculated by taking the pipe diameter of a and taking the wetness of the refrigerant inside the refrigerant amount adjustment container 5 on the vertical axis. This is what is shown. For example, in FIG. 5, if a branch pipe 7a with a diameter indicated by point h is used, the wetness of the refrigerant inside the refrigerant amount adjustment container 5 will be i under the design load conditions. As explained above, the wetness of the refrigerant inside the refrigerant amount adjusting container 5 can be set to any desired wetness by appropriately selecting the pipe diameter of the branch pipe 7a. As shown in Fig. 6, by providing fins 8 on the suction pipe 6 and the branch pipe 7a 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を通つて圧縮機1に吸い込まれることになり、
吸入管6の温度は、負荷が減少する前よりも、低
くなる。さらに、負荷が減少すれば、一般に、圧
縮機1から吐出された冷媒の温度は減少するため
分岐管7aの温度も減少する。このように、負荷
が減少すれば、冷媒量調節容器5を貫通している
吸入管6と分岐管7aとの温度の両方共に減少す
る。このため、冷媒量調節容器5の内部の飽和蒸
気状態の冷媒が凝縮するので、冷媒量調節容器5
の内部の冷媒の湿り度が大きくなり、冷媒の液相
の割合が大きくなる。その結果、冷媒量調節容器
5の内部に含まれる冷媒の質量は、負荷変動前と
比較すると、増加する。この増加した冷媒は、結
局、絞り装置3の途中の接続位置3aから、冷媒
回路中の冷媒が冷媒量調節容器5に流れこんだ冷
媒であるため、冷媒回路中の過剰な冷媒が除去さ
れたことになり、吸入管6の温度は上昇して前記
接続位置3aの温度と釣合う。 Next, the operation of the refrigerant amount adjusting device when the load fluctuates will be explained. First, considering the case where the load decreases, an excess amount of refrigerant will be circulating in the refrigerant circuit than the amount of refrigerant that allows the refrigeration system to exhibit its maximum capacity under this load condition, so the refrigerant with almost no superheat will be It 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 a liquid state,
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, so the temperature of the branch pipe 7a also decreases. In this way, when the load decreases, the temperatures of both the suction pipe 6 and the branch pipe 7a passing through the refrigerant amount adjustment container 5 decrease. Therefore, the refrigerant in the saturated vapor state inside the refrigerant amount adjustment container 5 condenses, so the refrigerant amount adjustment container 5
The wetness of the refrigerant inside 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 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
を通つて、圧縮機1に吸い込まれることになる。
つまり、吸入管6の温度は、負荷変動前よりも高
くなる。また、負荷が増加すれば、一般に、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
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 temperature of the suction pipe 6 becomes higher than before the load change. Additionally, as the load increases, the temperature of the refrigerant discharged from the compressor 1 generally increases;
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. Therefore, the refrigerant in the saturated liquid state inside the refrigerant amount adjustment container 5 evaporates, so the refrigerant amount adjustment container 5
The wetness of the refrigerant inside becomes smaller, and the proportion of the liquid phase of the refrigerant becomes smaller. 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 has flowed into the refrigerant circuit, which was in short supply. As the refrigerant is replenished, the temperature of the suction pipe 6 decreases and becomes balanced with the temperature of the connecting position 3a in the middle of the expansion device 3.
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
を貫通している吸入管6によつて冷媒量調節容器
5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5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。 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. Heat amount and refrigerant amount adjustment container 5
There is an amount of heat taken away from the refrigerant amount adjusting container 5 by the suction pipe 6 passing through the refrigerant amount adjusting container 5. Furthermore, in the present invention, the branch pipe 7a penetrating the refrigerant amount adjustment container 5
There is an amount of heat that enters the refrigerant amount adjustment container 5 from the inside.
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は負荷に対する吸入管6から
侵入する熱量の変化をあらわしている。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q6とを加えた
熱量になり、この全侵入熱量は、曲線q7であらわ
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 Figure 7, song q 4
represents the change in the amount of heat entering from the ambient air with respect to the load, and the curve q 5 represents the change in the amount of heat entering from the suction pipe 6 with respect to the load. moreover,
The curve q 6 represents 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 q 4 , q 5 , and q 6 , and this total amount of heat that enters is represented by the curve q 7 . Point y on the curve q 7 is the refrigerant amount adjustment container 5
This indicates that there is no amount of heat penetrating.
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7a
の管径を適当に選択することによつて、曲線q7上
の点y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 7a
By appropriately selecting the pipe diameter of , it is possible to position point y on curve q 7 between points m and n, which are the normal load range.
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7a
を冷媒量調節容器5に貫通させたことを特徴とし
ており、第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 explained earlier is that in FIG.
A branch pipe 7a branched from the discharge pipe 7 connecting the
It is characterized by passing through the refrigerant amount adjusting container 5, and in FIG. This is a distinctive feature.
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、第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とを連結する
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、吐出管7、あるいは、分岐管7aと吸入
管6とをそれぞれ冷媒量調節容器5と熱交換させ
ることである。故に、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5に接触さ
せるなどして、熱交換させるように配設させても
よい。 In the examples shown in FIGS. 3, 4, 6, and 8, a discharge pipe 7 connecting the compressor 1 and the condenser 2, or a branch pipe branched from the discharge pipe 7 7a and the suction pipe 6 are passed through the refrigerant amount adjustment container 5, but the meaning of this penetration is that the discharge pipe 7 or the branch pipe 7a and the suction pipe 6 are inserted into the refrigerant amount adjustment container 5. It is to exchange heat with 5. Therefore, the discharge pipe 7 or the branch pipe 7a and the suction pipe 6 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、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 has a compressor, a condenser, a throttling device, and an evaporator connected together in a ring, and the refrigerant amount adjusting container is placed in a connecting position in the middle of the throttling device or with the throttling device. A discharge pipe connected between the evaporator and the compressor and the condenser, or a branch pipe and a suction pipe branched from the discharge pipe are disposed in the refrigerant amount adjusting container for heat exchange. It is something that 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。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。 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. 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.
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、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……冷媒量調節容器、6…
…吸入管、7……吐出管、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. 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 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. 8 is a refrigeration diagram in another embodiment of the invention. It is a cycle diagram. 1... Compressor, 2... Condenser, 3... Throttle device, 4... Evaporator, 5... Refrigerant amount adjustment container, 6...
... Suction pipe, 7... Discharge pipe, 7a... Branch pipe.
Claims (1)
れ環状に連結し、さらに冷媒量調節容器を、前記
絞り装置と蒸発器との間における絞り装置の入口
側圧力より低い圧力となる位置に連絡し、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。1 A compressor, a condenser, a throttling device, and an evaporator are each connected in a ring, and a refrigerant amount adjustment container is connected to a position between the throttling device and the evaporator where the pressure is lower than the pressure on the inlet side of the throttling device. and a refrigerant in a refrigeration system in which a discharge pipe connecting the compressor and the condenser and a suction pipe connecting the evaporator and the compressor are disposed in the refrigerant amount adjusting container in a heat exchange manner. Amount control device.
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 JPS5845451A (en) | 1983-03-16 |
| JPS6240637B2 true 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) |
-
1981
- 1981-09-10 JP JP56143670A patent/JPS5845451A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5845451A (en) | 1983-03-16 |
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