JPS63247571A - Gas-liquid separator for refrigeration and air cooling - Google Patents

Gas-liquid separator for refrigeration and air cooling

Info

Publication number
JPS63247571A
JPS63247571A JP7901587A JP7901587A JPS63247571A JP S63247571 A JPS63247571 A JP S63247571A JP 7901587 A JP7901587 A JP 7901587A JP 7901587 A JP7901587 A JP 7901587A JP S63247571 A JPS63247571 A JP S63247571A
Authority
JP
Japan
Prior art keywords
gas
liquid
liquid separation
liquid separator
plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP7901587A
Other languages
Japanese (ja)
Other versions
JP2505194B2 (en
Inventor
敦雄 井上
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.)
Sanden Corp
Original Assignee
Sanden Corp
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 Sanden Corp filed Critical Sanden Corp
Priority to JP62079015A priority Critical patent/JP2505194B2/en
Publication of JPS63247571A publication Critical patent/JPS63247571A/en
Application granted granted Critical
Publication of JP2505194B2 publication Critical patent/JP2505194B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/23Separators

Landscapes

  • Applications Or Details Of Rotary Compressors (AREA)
  • Sorption Type Refrigeration Machines (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、アキームレータ、多効分離器等の冷凍・冷房
用気液分離器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a gas-liquid separator for refrigeration and cooling, such as an achimulator and a multi-effect separator.

〔従来の技術〕[Conventional technology]

冷凍又は冷房サイクルに用いられるアキュムレータは、
第5図に記号7で示すように蒸発器1゜と圧縮機8との
間に配置てれ、蒸発器10から吸入した気液混相冷媒を
液冷媒と蒸気冷媒とに分離し、液冷媒を一時溜めて蒸気
冷媒のみを圧縮機の吸入ポート(図示せず)に吸入でせ
る様にしている。9゛は凝縮器、11は膨張嵌溝である
。第7図はその種のアキュームレータの従来例を示し、
1は冷媒の入口管、2は蒸気出口管、3は容器である。
Accumulators used in refrigeration or cooling cycles are
It is placed between the evaporator 1° and the compressor 8, as shown by symbol 7 in FIG. The vapor refrigerant is temporarily stored so that only the vapor refrigerant can be sucked into the suction port (not shown) of the compressor. 9 is a condenser, and 11 is an expansion fitting groove. Figure 7 shows a conventional example of this type of accumulator.
1 is a refrigerant inlet pipe, 2 is a vapor outlet pipe, and 3 is a container.

また、冷凍又は冷房サイクルに用いられる多効分離器は
、第6図に記号12で示すように、凝縮器9又は受液器
(図示せず)出口に設けられる第1膨張機構13と、蒸
発器10人口に設けられる第2膨張機構14との間に配
置され、第1膨張機構13により気液混相となった冷媒
を吸入した後。
In addition, a multi-effect separator used in a refrigeration or cooling cycle includes a first expansion mechanism 13 provided at the outlet of the condenser 9 or a receiver (not shown), and an evaporator, as shown by symbol 12 in FIG. After inhaling the refrigerant which has become a gas-liquid mixed phase by the first expansion mechanism 13, the second expansion mechanism 14 is disposed between the second expansion mechanism 14 and the second expansion mechanism 14 provided at the bottom of the container 10.

液冷媒と蒸気冷媒とに分離し、そのうちの液冷媒を、一
時貯溜した後第2膨張機構14へ送出し。
The refrigerant is separated into a liquid refrigerant and a vapor refrigerant, and the liquid refrigerant is temporarily stored and then sent to the second expansion mechanism 14.

蒸気冷媒を圧縮機8のインジェクションポート(図示せ
ず)に吸入させる様にしている。第8図はその種の多効
分離器の従来例を示し、1は冷媒の入口管、2′は蒸気
出口管、3は容器、6は液出口管である。
The vapor refrigerant is sucked into an injection port (not shown) of the compressor 8. FIG. 8 shows a conventional example of this kind of multi-effect separator, in which 1 is a refrigerant inlet pipe, 2' is a steam outlet pipe, 3 is a container, and 6 is a liquid outlet pipe.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで、一般に冷房サイクル中の冷媒循環量が多いと
、気液分離器内に流入する気液混相冷媒の流速が大きく
なって、気液分離器内に貯溜する液冷媒は激しく攪拌で
れる。従来の気液分離器にあっては、これによってフォ
ーミングが発生しだシ、気液界面が大きくうねったシ、
あるいは又。
Generally, when the amount of refrigerant circulated during the cooling cycle is large, the flow rate of the gas-liquid multiphase refrigerant flowing into the gas-liquid separator increases, and the liquid refrigerant stored in the gas-liquid separator is vigorously agitated. In conventional gas-liquid separators, this causes forming, large undulations at the gas-liquid interface, and
Or again.

液冷媒の飛沫が気相空間を飛び交ったりして、液冷媒が
蒸気出口管へ流出し、圧縮機吸入ポート(アキュムレー
タの場合)あるいは、圧縮機インジェクションポート(
多効分離器の場合)に吸入されてしまうおそれが高かっ
゛た。こうして圧縮機内に液冷媒が吸入されると、湿り
圧縮又は液圧縮の状態となり、圧縮機から異音が発生し
たり、圧縮機の弁が破損したシするという問題や、冷房
サイクルの効率の低下による冷房能力の低下を招くとい
う問題が起きてしまう。一方、この問題の解決を図って
液冷媒が蒸気出口管へ流出するのを防ごうとすると、従
来技術のままでは気液分離器の容積を大きくしなければ
ならないという別の問題が発生してしまう。
The droplets of liquid refrigerant fly around in the gas phase space, and the liquid refrigerant flows out into the vapor outlet pipe, and is connected to the compressor suction port (in the case of an accumulator) or the compressor injection port (in the case of an accumulator).
In the case of multi-effect separators), there was a high risk of inhalation. When liquid refrigerant is sucked into the compressor in this way, it becomes wet compression or liquid compression, causing problems such as abnormal noise from the compressor, damage to the compressor valve, and a decrease in the efficiency of the cooling cycle. A problem arises in that the cooling capacity is reduced due to On the other hand, if we try to solve this problem and prevent the liquid refrigerant from flowing into the vapor outlet pipe, another problem arises in that the volume of the gas-liquid separator must be increased using the conventional technology. Put it away.

〔問題点を解決するだめの手段〕[Failure to solve the problem]

本発明に係る気液分離器においては1分離器に流入する
気液混相冷媒の流れる方向に逆らうように、複数枚の気
液分離板を前記流れの方向に浴って段階的に間隔をとっ
て配し、蒸気出口管の開口端が前記複数枚の分離板の直
下に設けられている。
In the gas-liquid separator according to the present invention, a plurality of gas-liquid separation plates are arranged at stepwise intervals in the direction of flow so as to oppose the flow direction of the gas-liquid multiphase refrigerant flowing into one separator. and the open end of the steam outlet pipe is provided directly below the plurality of separation plates.

〔作用〕[Effect]

気液分離器に流入する気液混相冷媒の流速が段階的に流
れに沿って設けた気液分離板によって緩和てれフォーミ
ング等を防止する。
The flow velocity of the gas-liquid multiphase refrigerant flowing into the gas-liquid separator is relaxed by the gas-liquid separation plate provided along the flow in stages to prevent foaming and the like.

〔実施例〕〔Example〕

以下2本発明の実施例を示す図面により説明する。 DESCRIPTION OF THE PREFERRED EMBODIMENTS Two embodiments of the present invention will be explained below with reference to drawings.

第1図は1本発明をアキュムレータに適用した実施例を
示す。このアキュームレータにおいて。
FIG. 1 shows an embodiment in which the present invention is applied to an accumulator. In this accumulator.

気液分離に関する機構は、容器3内に配した円板状の第
1の気液分離板4と、リング状の第2の気液分離板5を
含む。第1の気液分離板4の上部。
The mechanism related to gas-liquid separation includes a disk-shaped first gas-liquid separation plate 4 and a ring-shaped second gas-liquid separation plate 5 arranged inside the container 3. The upper part of the first gas-liquid separation plate 4.

即ち、容器上部中央には、第1の気液分離板4と直交開
口する冷媒の入口管1が備えられている。
That is, a refrigerant inlet pipe 1 opening perpendicular to the first gas-liquid separation plate 4 is provided at the center of the upper part of the container.

冷媒の入口管1は、容器上面のほぼ中央に開口している
。第1の気液分離板4の直下には、蒸気出口管2が開口
している。
The refrigerant inlet pipe 1 opens approximately at the center of the top surface of the container. A steam outlet pipe 2 is opened directly below the first gas-liquid separation plate 4 .

第1の気液分離板4は、入口管lの開口端より下方数咽
〜土数閲の所に、容器側内壁と数1の隙間を保ち、しか
も入口管1の開口端と直交するよう容器3の上部内面に
保持されている。第2の気液分離板5は、第1の気液分
離板4よシ下方に置かれ、容器側内壁に密着保持されて
いる。この第2の気液分離板5はその中央部が大きく開
口しており、リング状を呈している。そしてこの第2の
気液分離板5の開口径は、第1の気液分離板4の外径と
同等若しくは、若干小さめとしである。
The first gas-liquid separation plate 4 is located a few feet to a few feet below the opening end of the inlet pipe 1, maintaining a gap of several 1 from the inner wall on the container side, and perpendicular to the opening end of the inlet pipe 1. It is held on the upper inner surface of the container 3. The second gas-liquid separation plate 5 is placed below the first gas-liquid separation plate 4 and is held in close contact with the inner wall of the container. This second gas-liquid separation plate 5 has a large opening in the center and has a ring shape. The opening diameter of the second gas-liquid separation plate 5 is equal to or slightly smaller than the outer diameter of the first gas-liquid separation plate 4.

蒸気出口管2は、容器3の底面中央部を貫通し。The steam outlet pipe 2 passes through the center of the bottom surface of the container 3.

第2の気液分離板5よシ上でしかも第1の気液分離板4
の直下に開口している。さらにこの蒸気出口管2には、
潤滑油の循環を考慮して容器3内底部空間と連通ずる小
径孔30が形成され、容器内底部に溜った液をわずか吸
入するようになっている。
Above the second gas-liquid separation plate 5 and above the first gas-liquid separation plate 4
It opens directly below. Furthermore, in this steam outlet pipe 2,
In consideration of the circulation of lubricating oil, a small diameter hole 30 communicating with the inner bottom space of the container 3 is formed to suck in a small amount of the liquid accumulated in the inner bottom of the container.

第1図に示したアキュームレータは第5図のアキューム
レータ7として使用し得る。第1図及び第4図を参照し
て、圧縮機8が作動し冷凍回路が作動状態となると、蒸
発器10からの気液混相冷媒が冷媒の入口管1を介しア
キ−ムレ−タフ内部に導入てれる。このとき、冷媒の入
口管1は、第1の気液分離板4に対向するよう開口して
いるので、流入した気液混相冷媒は第1の気液分離板4
にぶつかシ、その運動エネルギーが、緩和烙れる。
The accumulator shown in FIG. 1 can be used as accumulator 7 in FIG. Referring to FIGS. 1 and 4, when the compressor 8 is activated and the refrigeration circuit is activated, the gas-liquid multiphase refrigerant from the evaporator 10 enters the inside of the Achiemlet Tough through the refrigerant inlet pipe 1. It can be introduced. At this time, since the refrigerant inlet pipe 1 is opened to face the first gas-liquid separation plate 4, the inflowing gas-liquid multiphase refrigerant passes through the first gas-liquid separation plate 4.
When it hits, the kinetic energy is relaxed and heated.

次に、気液混相冷媒は、第1の気液分離板4の外周と容
器3の内壁との隙間から下方に向かって流れ、第2の気
液分離板5にぶつかる。気液混相冷媒の流入速度が大き
い場合、主に、この第2の気液分離板5により気液分離
がな石れ、液分は液滴となって落下し、蒸気は、蒸気出
口管2の開口端より圧縮機8へ導かれる。一方、気液混
相冷媒の流入速度が小さい場合は、主に第1の気液分離
板4によシ気液分離がなされる。以上のように、第1及
び第2の気液分離板4,5を用いることにより、液入す
る気液混相冷媒の運動エネルギーを減少嘔せているので
、フォーミングや液冷媒の飛沫の発生を防止できる。
Next, the gas-liquid multiphase refrigerant flows downward through the gap between the outer periphery of the first gas-liquid separation plate 4 and the inner wall of the container 3, and collides with the second gas-liquid separation plate 5. When the inflow speed of the gas-liquid multiphase refrigerant is high, the gas-liquid separation is mainly caused by this second gas-liquid separation plate 5, the liquid becomes droplets and falls, and the steam is transferred to the vapor outlet pipe 2. is guided to the compressor 8 from the open end of the . On the other hand, when the inflow speed of the gas-liquid multiphase refrigerant is low, gas-liquid separation is mainly performed by the first gas-liquid separation plate 4. As described above, by using the first and second gas-liquid separation plates 4 and 5, the kinetic energy of the gas-liquid multiphase refrigerant entering the liquid is reduced, thereby preventing forming and splashing of the liquid refrigerant. It can be prevented.

以上の説明では第1及び第2の気液分離板を互いに別体
としたが1例えば第2図に示すように一体構造とした気
液分離板40でも同様な効果を期待することができる。
In the above description, the first and second gas-liquid separation plates are separate from each other; however, similar effects can be expected even if the gas-liquid separation plate 40 is integrally constructed as shown in FIG. 2, for example.

また、上述の実施例では、2個の気液分離板4゜5を用
いて気液分離を行っているが、気液混相冷媒の流入速度
等を勘案して3個以上の気液分離板を用いてもよい。第
3図にその実施例を示す。この実施例では、冷媒の入口
管1より流入した気液混相冷媒は先ず、容器3の上部に
当たる。気液混相冷媒は次に第1の気液分離板4.第2
の気液分離板5.及び第3の気液分離板16と順次当た
る。
In the above embodiment, two gas-liquid separation plates 4.5 are used to perform gas-liquid separation, but in consideration of the inflow speed of the gas-liquid mixed phase refrigerant, three or more gas-liquid separation plates may be used. may also be used. An example is shown in FIG. In this embodiment, the gas-liquid multiphase refrigerant flowing from the refrigerant inlet pipe 1 first hits the upper part of the container 3. The gas-liquid multiphase refrigerant is then passed through the first gas-liquid separation plate 4. Second
Gas-liquid separation plate 5. and the third gas-liquid separation plate 16 in sequence.

こうして気液分離がなされ、蒸気冷媒は蒸気出口管2の
開口部よシ流出し、液冷媒は下方へ滴下する。この実施
例においては、先の実施例と同等若しくはそれ以上に気
液分離効率が良い。
Gas-liquid separation is thus performed, the vapor refrigerant flows out through the opening of the vapor outlet pipe 2, and the liquid refrigerant drips downward. In this embodiment, the gas-liquid separation efficiency is equal to or higher than that of the previous embodiment.

第2の気液分離板5を冷媒に対しぬれ性の良い材料にて
作ることは好ましい。これによれば、液冷媒が分離板で
はね返り、飛沫になるのを防止できるため、蒸気出口管
2の開口端から液冷媒の飛沫が吸入されるようなことが
なくなる。
It is preferable that the second gas-liquid separation plate 5 is made of a material that has good wettability with the refrigerant. According to this, since the liquid refrigerant can be prevented from bouncing off the separation plate and turning into droplets, the droplets of the liquid refrigerant will not be sucked in from the open end of the vapor outlet pipe 2.

また、第2の気液分離板5として、小径孔、若しくはス
リット状孔を施した二つのリング状の板挟 部材に吸湿物質をtみこんだものを用いてもよい。
Further, as the second gas-liquid separation plate 5, a structure in which a moisture-absorbing substance is filled between two ring-shaped plate members provided with small-diameter holes or slit-like holes may be used.

これによれば冷媒中の水分を吸収できるようになる。According to this, moisture in the refrigerant can be absorbed.

嘔らにこの二つのリング状の板部材表面に冷媒のぬれ性
の良い材料をコーティングし、液冷媒の飛沫の発生も防
ぐようにすることも好ましい。
It is also preferable to coat the surfaces of these two ring-shaped plate members with a material that has good refrigerant wettability to prevent splashing of liquid refrigerant.

ここまでは本発明をアキュムレータに適用した例につい
て説明したが2本発明が第4図に示すような多動分離器
に適用できることは言うまでもない。この場合、圧縮機
インジェクシコンポート(図示せず)に連通ずる蒸気出
口管2′は、その開口端を第2の気液分離板5よりも上
でしかも第1の気液分離板4の直下に設けている。第2
の膨張機構に連通ずる液出口管6は、その開口端を容器
3の内部の最下部空間に設けている。
Up to this point, an example in which the present invention is applied to an accumulator has been described, but it goes without saying that the present invention can also be applied to a hyperactive separator as shown in FIG. In this case, the vapor outlet pipe 2' communicating with the compressor injection component port (not shown) has its open end located above the second gas-liquid separation plate 5 and directly below the first gas-liquid separation plate 4. It is set up in Second
A liquid outlet pipe 6 communicating with the expansion mechanism has its open end located in the lowest space inside the container 3.

〔発明の効果〕〔Effect of the invention〕

以上述べたように2本発明に係る気液分離器においては
1分離器に流入する気液混相冷媒の流れる方向に逆らう
ように、複数枚の気液分離板を前記流れの方向に溢って
段階的に間隔をとって配し。
As described above, in the gas-liquid separator according to the present invention (1), a plurality of gas-liquid separation plates are arranged so as to overflow in the direction of flow of the gas-liquid multiphase refrigerant flowing into the separator, so as to counteract the flow direction of the gas-liquid multiphase refrigerant. Arranged at gradual intervals.

蒸気出口管の開口端を前記複数枚の分離板の直下に設け
だので、気液分離器に流入する気液混相冷媒の流速が、
気液分離板によって緩和されフォーミングや液冷媒の飛
沫の発生を防止できる。その上、気液分離を省スペース
にて促進式せることができる。また容器の下方に溜って
いる液冷媒のフォーミングや、飛沫の発生を防止し、圧
縮機へ液冷媒が流入するのを防ぎ、液圧縮、湿シ圧縮に
よる種々の不具合を解消することが可能となる。
Since the open end of the vapor outlet pipe is provided directly below the plurality of separation plates, the flow rate of the gas-liquid multiphase refrigerant flowing into the gas-liquid separator is
The gas-liquid separation plate alleviates this problem and prevents forming and splashing of liquid refrigerant. Moreover, gas-liquid separation can be facilitated in a space-saving manner. It also prevents the liquid refrigerant that accumulates at the bottom of the container from forming and splashing, and prevents the liquid refrigerant from flowing into the compressor, making it possible to eliminate various problems caused by liquid compression and wet compression. Become.

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

第1図は本発明の一実施例によるアキニームレータ縦断
面図である。第2図は本発明の他の実施例によるアキニ
ームレータに使用される気液分離板を示し、(a)は平
面図、(b)は正面図である。第3図は本発明のさらに
他の実施例によるアキニームレータの縦断面図である。 第4図は本発明のさらに他の実施例による多効分離器の
縦断面図である。 第5図はアキュームレータを用いた一般的な冷凍サイク
ルを示すブロック図である。第6図は多効分離器を用い
た一般的な冷凍サイクルを示すブロック図である。第7
図は従来のアキュームレータの縦断面図である。第8図
は従来の多効分離器の縦断面図である。 図中、1:冷媒の入口管、2;蒸気出口管、3:容器、
4:第1の気液分離板、5:第2の気液分離板、6:液
出口管、7:アキエムレータ、8:圧縮機、9:凝縮器
、10:蒸発器、11:膨張機構、12:多動分離器、
13:第1膨張機構。 14:第2膨張機構、15:潤滑油戻し通路。 16:第3の気液分離板。 第1図 マ 第3図 第7図 ↓
FIG. 1 is a longitudinal cross-sectional view of an akinimulator according to an embodiment of the present invention. FIG. 2 shows a gas-liquid separation plate used in an akinimulator according to another embodiment of the present invention, in which (a) is a plan view and (b) is a front view. FIG. 3 is a longitudinal sectional view of an akinimulator according to still another embodiment of the present invention. FIG. 4 is a longitudinal sectional view of a multi-effect separator according to still another embodiment of the present invention. FIG. 5 is a block diagram showing a general refrigeration cycle using an accumulator. FIG. 6 is a block diagram showing a general refrigeration cycle using a multi-effect separator. 7th
The figure is a longitudinal sectional view of a conventional accumulator. FIG. 8 is a longitudinal sectional view of a conventional multi-effect separator. In the figure, 1: refrigerant inlet pipe, 2: vapor outlet pipe, 3: container,
4: First gas-liquid separation plate, 5: Second gas-liquid separation plate, 6: Liquid outlet pipe, 7: Akie emulator, 8: Compressor, 9: Condenser, 10: Evaporator, 11: Expansion mechanism, 12: Hyperactive separator,
13: First expansion mechanism. 14: second expansion mechanism, 15: lubricating oil return passage. 16: Third gas-liquid separation plate. Figure 1 Figure 3 Figure 7 ↓

Claims (8)

【特許請求の範囲】[Claims] (1)外部から流入する気液混相冷媒を密閉容器内に導
く入口部と,密閉容器内の蒸気を外部に排出するための
,容器内部空間に開口端を有する蒸気出口管とを設け,
密閉容器巾に流入する気液混相冷媒を,密閉容器中にて
蒸気と液体に分離する冷凍・冷房用気液分離器において
,流入した気液混相冷媒の流れの方向を横切る様に,複
数の気液分離板を,前記冷媒の流れの方向に沿って間隔
を採り段階的に配するとともに,前記蒸気出口管の開口
端を,前記複数の気液分離板のいずれかの直下に設けた
事を特徴とする,冷凍・冷房用気液分離器。
(1) Providing an inlet section for guiding the gas-liquid multiphase refrigerant flowing in from the outside into the closed container, and a vapor outlet pipe having an open end in the internal space of the container for discharging the steam inside the closed container to the outside;
In a gas-liquid separator for refrigeration and cooling, which separates gas-liquid multiphase refrigerant flowing into the width of a sealed container into vapor and liquid, multiple The gas-liquid separation plates are arranged in stages at intervals along the flow direction of the refrigerant, and the open end of the vapor outlet pipe is provided directly below any one of the plurality of gas-liquid separation plates. A gas-liquid separator for refrigeration and air conditioning, featuring:
(2)前記複数の気液分離板が,前記気液分離器上部か
ら下方に向って流入する気液混相冷媒の流れを横切るよ
うに前記気液分離器の内壁面と数mmの隙間をもって配
された第1気液分離板と,前記第1気液分離板の下方に
配され,気液分離器内壁面と密着し,その中央に前記第
1気液分離板の径より小径または同等の開口をもち前記
第1気液分離板とほぼ平行をなす第2の気液分離板とか
らなるとともに,前記蒸気出口管の開口端を,前記第1
の気液分離板直下に開口した特許請求の範囲第(1)項
記載の冷凍・冷房用気液分離器。
(2) The plurality of gas-liquid separators are arranged with a gap of several mm from the inner wall surface of the gas-liquid separator so as to cross the flow of the gas-liquid multiphase refrigerant flowing downward from the upper part of the gas-liquid separator. is arranged below the first gas-liquid separation plate, is in close contact with the inner wall surface of the gas-liquid separator, and has a diameter smaller than or equivalent to that of the first gas-liquid separation plate in the center. a second gas-liquid separation plate having an opening and substantially parallel to the first gas-liquid separation plate;
A gas-liquid separator for freezing and cooling according to claim (1), which opens directly below the gas-liquid separator plate.
(3)前記複数の気液分離板が一体構造となっているこ
とを特徴とする特許請求の範囲第(1)項記の冷凍・冷
房用気液分離器。
(3) The gas-liquid separator for freezing and cooling according to claim (1), wherein the plurality of gas-liquid separation plates have an integral structure.
(4)前記複数の気液分離板のうち少なくとも一つの気
液分離板がぬれ性のよい材料にて作られている特許請求
の範囲第(1)項記載の冷凍・冷房用気液分離器。
(4) A gas-liquid separator for freezing and cooling according to claim (1), wherein at least one gas-liquid separation plate among the plurality of gas-liquid separation plates is made of a material with good wettability. .
(5)前記複数の気液分離板のうち少なくとも一つの気
液分離板は,多数の孔を有した複数枚の板部材と,これ
らの板部材の相互間にはさまれたぬれ性のよい材料とを
含むものである特許請求の範囲第(1)項記載の冷凍・
冷房用気液分離器。
(5) At least one of the plurality of gas-liquid separation plates includes a plurality of plate members having a large number of holes, and a material with good wettability sandwiched between these plate members. The refrigeration method according to claim (1), which includes the
Gas-liquid separator for cooling.
(6)前記板部材の孔は丸孔である特許請求の範囲第(
5)項記載の冷凍・冷房用気液分離器。
(6) The hole in the plate member is a round hole.
5) Gas-liquid separator for freezing and cooling.
(7)前記板部材の孔はスリット状のものである特許請
求の範囲第(5)項記載の冷凍・冷房用気液分離器。
(7) A gas-liquid separator for freezing and cooling according to claim (5), wherein the hole in the plate member is in the form of a slit.
(8)前記板部材はその表面にぬれ性の良い材料をコー
ティングしたものである特許請求の範囲第(5)項記載
の冷凍・冷房用気液分離器。
(8) A gas-liquid separator for freezing and cooling according to claim (5), wherein the surface of the plate member is coated with a material having good wettability.
JP62079015A 1987-03-31 1987-03-31 Gas-liquid separator for freezing and cooling Expired - Lifetime JP2505194B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62079015A JP2505194B2 (en) 1987-03-31 1987-03-31 Gas-liquid separator for freezing and cooling

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62079015A JP2505194B2 (en) 1987-03-31 1987-03-31 Gas-liquid separator for freezing and cooling

Publications (2)

Publication Number Publication Date
JPS63247571A true JPS63247571A (en) 1988-10-14
JP2505194B2 JP2505194B2 (en) 1996-06-05

Family

ID=13678119

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62079015A Expired - Lifetime JP2505194B2 (en) 1987-03-31 1987-03-31 Gas-liquid separator for freezing and cooling

Country Status (1)

Country Link
JP (1) JP2505194B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011122783A (en) * 2009-12-11 2011-06-23 Fuji Koki Corp Accumulator and method for manufacturing the same
WO2013076971A1 (en) * 2011-11-22 2013-05-30 パナソニック株式会社 Gas-liquid separator and refrigeration cycle device

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS537715U (en) * 1976-07-06 1978-01-23
JPS56139972U (en) * 1980-03-21 1981-10-22

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS537715U (en) * 1976-07-06 1978-01-23
JPS56139972U (en) * 1980-03-21 1981-10-22

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011122783A (en) * 2009-12-11 2011-06-23 Fuji Koki Corp Accumulator and method for manufacturing the same
WO2013076971A1 (en) * 2011-11-22 2013-05-30 パナソニック株式会社 Gas-liquid separator and refrigeration cycle device

Also Published As

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JP2505194B2 (en) 1996-06-05

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