JP2505194B2 - Gas-liquid separator for freezing and cooling - Google Patents
Gas-liquid separator for freezing and coolingInfo
- Publication number
- JP2505194B2 JP2505194B2 JP62079015A JP7901587A JP2505194B2 JP 2505194 B2 JP2505194 B2 JP 2505194B2 JP 62079015 A JP62079015 A JP 62079015A JP 7901587 A JP7901587 A JP 7901587A JP 2505194 B2 JP2505194 B2 JP 2505194B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquid
- plate
- liquid separation
- separation 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.)
- Expired - Lifetime
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General 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
- F25B2400/23—Separators
Landscapes
- Sorption Type Refrigeration Machines (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Applications Or Details Of Rotary Compressors (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,アキュムレータ,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。TECHNICAL FIELD The present invention relates to a gas-liquid separator for refrigeration / cooling such as an accumulator and a multi-effect separator.
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10と圧縮機8と
の間に配置され,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)に吸入させ
る様にしている。9は凝縮器,11は膨張機構である。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。The accumulator used for the refrigeration or cooling cycle is arranged between the evaporator 10 and the compressor 8 as shown by symbol 7 in FIG. 5, and the gas-liquid mixed phase refrigerant sucked from the evaporator 10 is used as a liquid refrigerant and a vapor refrigerant. The liquid refrigerant is temporarily collected and only the vapor refrigerant is sucked into the suction port (not shown) of the compressor. Reference numeral 9 is a condenser, and 11 is an expansion mechanism. FIG. 7 shows a conventional example of such an 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入口に設けられる第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,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,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。Further, the multi-effect separator used in the refrigeration or cooling cycle is, as shown by symbol 12 in FIG. 6, a condenser 9 or a first expansion mechanism 13 provided at the outlet of a liquid receiver (not shown), and an evaporator. The first expansion mechanism 13 is arranged between the second expansion mechanism 14 provided at the inlet of the container 10 and sucks the gas-liquid mixed phase refrigerant, and then separates it into a liquid refrigerant and a vapor refrigerant. Is temporarily stored and then sent to the second expansion mechanism 14 so that the vapor refrigerant is sucked into the injection port (not shown) of the compressor 8. FIG. 8 shows a conventional example of such a multi-effect separator. 1 is a refrigerant inlet pipe, 2'is a vapor outlet pipe, 3 is a container, and 6 is a liquid outlet pipe.
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撹拌
される。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たり,気液界面が大きくうねった
り,あるいは又,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りするとい
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。By the way, generally, when the refrigerant circulation amount in the cooling cycle is large, the flow velocity of the gas-liquid mixed phase refrigerant flowing into the gas-liquid separator increases, and the liquid refrigerant stored in the gas-liquid separator is vigorously stirred. In the conventional gas-liquid separator, this causes foaming, the gas-liquid interface is greatly undulated, or the liquid refrigerant splashes in the gas phase space. There is a high risk that it will flow out to the compressor suction port (in case of accumulator) or the compressor injection port (in case of multi-effect separator). When the liquid refrigerant is sucked into the compressor in this manner, the liquid refrigerant enters a wet or liquid compression state, which causes abnormal noise from the compressor and damage to the valve of the compressor, and reduces the efficiency of the cooling cycle. This causes a problem that the cooling capacity is deteriorated due to. On the other hand, in order to solve this problem and prevent the liquid refrigerant from flowing out to the vapor outlet pipe, another problem occurs that the volume of the gas-liquid separator must be increased with the conventional technology. I will end up.
本発明に係る気液分離器においては、該気液分離器の
上部から下方に向かって流入する前記気液混相冷媒が衝
突するように第1、第2及び第3の気液分離板を前記流
れの方向に沿って間隔を取り、前記気液混相冷媒が前記
第1の気液分離板の板体面を介してその外周より、前記
第2の気液分離板の板体面を介してその開口、又は前記
開口から前記第3の気液分離板の板体面を介してその外
周へと順次段階的に流れるように配置し、蒸気出口管の
開口端が前記第1又は第3の気液分離板の直下に設けら
れている。In the gas-liquid separator according to the present invention, the first, second and third gas-liquid separation plates are provided so that the gas-liquid mixed phase refrigerant flowing downward from the upper part of the gas-liquid separator collides with the gas-liquid separator. A space is provided along the flow direction, and the gas-liquid mixed-phase refrigerant is opened from the outer periphery thereof through the plate surface of the first gas-liquid separation plate through the plate surface of the second gas-liquid separation plate. Alternatively, it is arranged so as to flow stepwise from the opening to the outer periphery thereof through the plate surface of the third gas-liquid separation plate, and the opening end of the vapor outlet pipe is the first or third gas-liquid separation. It is provided just below the board.
気液分離器の上部から下方に向かって流入する気液混
相冷媒の流速が順次段階的に流れに沿って設けた第1、
第2及び第3の気液分離板によって緩和されフォーミン
グ等を防止する。First, the flow velocity of the gas-liquid mixed phase refrigerant flowing downward from the upper part of the gas-liquid separator is provided step by step along the flow,
The second and third gas-liquid separation plates alleviate the formation and prevent forming and the like.
以下,本発明の実施例を示す図面により説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図は,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,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,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。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,蒸気出力管
2が開口している。FIG. 1 shows an embodiment in which the present invention is applied to an accumulator. In this accumulator, 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 in the container 3. In the upper part of the first gas-liquid separation plate 4, that is, in the center of the upper part of the container, a refrigerant inlet pipe 1 that is orthogonal to the first gas-liquid separation plate 4 is provided. The refrigerant inlet pipe 1 is open at approximately the center of the upper surface of the container. A steam output pipe 2 is opened immediately below the first gas-liquid separation plate 4.
第1の気液分離板4は,入口管1の開口端より下方数
mm〜十数mmの所に,容器側内壁と数mm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より下方に置かれ,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,若干小さめとしてある。The number of the first gas-liquid separating plate 4 is lower than the opening end of the inlet pipe 1.
It is held on the inner surface of the upper part of the container 3 so as to keep a gap of several mm from the inner wall of the container at a position of mm to ten and a few mm and to be orthogonal to the open end of the inlet pipe 1. The second gas-liquid separation plate 5 is placed below the first gas-liquid separation plate 4, and is closely held by the inner wall of the container. The second gas-liquid separation plate 5 has a large opening at the center and has a ring shape. And this second
The opening diameter of the gas-liquid separating plate 5 is equal to or slightly smaller than the outer diameter of the first gas-liquid separating plate 4.
蒸気出口管2は,容器3の底面中央部を貫通し,第2
の気液分離板5より上でしかも第1の気液分離板4の直
下に開口している。さらにこの蒸気出力管2には,潤滑
油の循環を考慮して容器3内底部空間と連通する小径孔
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。The steam outlet pipe 2 passes through the center of the bottom surface of the container 3 and
Above the gas-liquid separating plate 5 and directly below the first gas-liquid separating plate 4. Furthermore, the steam output pipe 2 has a small diameter hole communicating with the inner bottom space of the container 3 in consideration of the circulation of lubricating oil.
30 is formed so that a little of the liquid accumulated at the bottom of the container can be inhaled.
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5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
キュムレータ7内部に導入される。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
にぶつかり,その運動エネルギーが,緩和される。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
なされ,液分は液滴となって第2の気液分離板5の中央
部開口より落下し,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により気液分離
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
エネルギーを減少させているので,フォーミングや液冷
媒の飛沫の発生を防止できる。The accumulator shown in FIG. 1 can be used as the accumulator 7 in FIG. Referring to FIG. 1 and FIG. 5, when the compressor 8 is activated and the refrigeration circuit is activated,
The gas-liquid mixed phase refrigerant from the evaporator 10 is introduced into the accumulator 7 through the refrigerant inlet pipe 1. At this time, since the refrigerant inlet pipe 1 is opened so as to face the first gas-liquid separation plate 4, the inflowing gas-liquid mixed phase refrigerant flows into the first gas-liquid separation plate 4
It hits and its kinetic energy is relaxed. Next, the gas-liquid mixed phase refrigerant flows downward from the gap between the outer periphery of the first gas-liquid separation plate 4 and the inner wall of the container 3 and hits the second gas-liquid separation plate 5. When the inflow velocity of the gas-liquid mixed phase refrigerant is high, the gas-liquid separation is mainly performed by the second gas-liquid separation plate 5, and the liquid component becomes droplets and the central opening of the second gas-liquid separation plate 5 is formed. Further falling, the steam is guided to the compressor 8 from the opening end of the steam outlet pipe 2. On the other hand, when the inflow velocity of the gas-liquid mixed phase refrigerant is low, the gas-liquid separation is mainly performed by the first gas-liquid separation plate 4. As described above, the first and second gas-liquid separation plates
By using 4,5, since the kinetic energy of the gas-liquid mixed-phase refrigerant entering the liquid is reduced, it is possible to prevent the formation of foaming and the generation of droplets of the liquid refrigerant.
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,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。
これにより、容器3への気液分離板40の組付を容易に行
うことができる。In the above description, the first and second gas-liquid separation plates are separate from each other, but the same effect can be expected with the gas-liquid separation plate 40 having an integrated structure as shown in FIG. 2, for example.
Thereby, the gas-liquid separation plate 40 can be easily attached to the container 3.
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の板体面
に衝突し,その外周を通ってさらに第2の気液分離板5
の板体面に衝突し、その中央部開口を通ってそして第3
の気液分離板16の板体面に衝突する。こうして気液分離
がなされ、蒸気冷媒は蒸気出口管2の開口部より流出
し、液冷媒は第3の気液分離板の外周より下方へ滴下す
る。この実施例においては,先の実施例と同様若しくは
それ以上に気液分離効率が良い。Further, in the above-described embodiment, the gas-liquid separation is performed using the two gas-liquid separation plates 4 and 5, but three or more gas-liquid separation plates are taken into consideration in consideration of the inflow speed of the gas-liquid mixed phase refrigerant. May be used. Third
An example is shown in the figure. In this embodiment, the gas-liquid mixed phase refrigerant that has flowed in through the refrigerant inlet pipe 1 first hits the upper portion of the container 3. The gas-liquid mixed-phase refrigerant then collides with the plate surface of the first gas-liquid separation plate 4, passes through the outer periphery thereof, and further passes through the second gas-liquid separation plate 5.
Colliding with the plate surface, through its central opening and
It collides with the plate surface of the gas-liquid separation plate 16. In this way, gas-liquid separation is performed, the vapor refrigerant flows out from the opening of the vapor outlet pipe 2, and the liquid refrigerant drops downward from the outer periphery of the third gas-liquid separation plate. In this embodiment, the gas-liquid separation efficiency is higher than that of the previous embodiment or higher.
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 having good wettability with respect to the refrigerant. According to this, it is possible to prevent the liquid refrigerant from splashing and splashing on the separation plate, so that the droplets of the liquid refrigerant are not sucked from the opening 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部材に吸湿物
質を挾みこんだものを用いてもよい。これによれば冷媒
中の水分を吸収できるようになる。Further, as the second gas-liquid separation plate 5, two ring-shaped plate members having small-diameter holes or slit-shaped holes and a hygroscopic substance sandwiched therein may be used. According to this, it becomes possible to absorb the water in the refrigerant.
さ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。Further, it is also preferable to coat the surfaces of the two ring-shaped plate members with a material having good wettability of the refrigerant so as to prevent the liquid refrigerant from splashing.
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,本発明が第4図に示すような多効分離
器に適用できることは言うまでもない。この場合,圧縮
機インジェクションポート(図示せず)に連通する蒸気
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の膨張機構に連通する液出口管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 be applied to a multi-effect separator as shown in FIG. In this case, the vapor outlet pipe 2 ′ communicating with the compressor injection port (not shown) has its open end above the second gas-liquid separation plate 5 and directly below the first gas-liquid separation plate 4. It is provided. The liquid outlet pipe 6 communicating with the second expansion mechanism has the open end provided in the lowermost space inside the container 3.
以上述べたように、本発明に係る気液分離器において
は、該気液分離器の上部から下方に向かって流入する前
記気液混相冷媒が衝突するように第1、第2及び第3の
気液分離板を前記流れの方向に沿って間隔を取り、前記
気液混相冷媒が前記第1の気液分離板の板体面を介して
その外周より、前記第2の気液分離板の板体面を介して
その開口、又は前記開口から前記第3の気液分離板の板
体面を介してその外周へと順次段階的に流れるように配
置し、蒸気出口管の開口端が前記第1又は第3の気液分
離板の直下に設けられているので、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させることができ
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,湿り圧縮による種々の不具合を解消す
ることが可能となる。更に、第1乃至第2又は第1乃至
第3の気液分離板を一体構造としたもでは、気液分離器
の組立時に、一度に容易に第1、第2及び第3の気液分
離板を組付けることができる。As described above, in the gas-liquid separator according to the present invention, the first, second and third gas-liquid mixed phase refrigerants flowing downward from the upper part of the gas-liquid separator collide with each other. The gas-liquid separation plate is spaced along the flow direction, and the gas-liquid mixed-phase refrigerant passes through the plate surface of the first gas-liquid separation plate from its outer periphery to the plate of the second gas-liquid separation plate. It is arranged so as to flow stepwise from the opening through the body surface, or from the opening to the outer periphery through the plate body surface of the third gas-liquid separating plate, and the opening end of the vapor outlet pipe is the first or Since it is provided directly below the third gas-liquid separation plate, the flow velocity of the gas-liquid mixed phase refrigerant flowing into the gas-liquid separator is moderated by the gas-liquid separation plate, and it is possible to prevent the formation of foaming and the splash of liquid refrigerant. Moreover, gas-liquid separation can be promoted in a small space. Further, it is possible to prevent the liquid refrigerant accumulated below the container from forming and splashing, to prevent the liquid refrigerant from flowing into the compressor, and to solve various problems due to liquid compression and wet compression. . Further, even if the first to second or the first to third gas-liquid separation plates are integrated, the first, second and third gas-liquid separation can be easily performed at one time when the gas-liquid separator is assembled. The board can be assembled.
第1図は本発明の一実施例によるアキュームレータ縦断
面図である。第2図は本発明の他の実施例によるアキュ
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ュ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:アキュム
レータ,8:圧縮機,9:凝縮器,10:蒸発器,11:膨張機構,12:
多効分離器,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。FIG. 1 is a vertical sectional view of an accumulator according to an embodiment of the present invention. FIG. 2 shows a gas-liquid separating plate used in an accumulator according to another embodiment of the present invention, (a) is a plan view and (b) is a front view. FIG. 3 is a vertical sectional view of an accumulator according to still another embodiment of the present invention.
FIG. 4 is a vertical sectional view of a multi-effect separator according to 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. FIG. 7 is a vertical sectional view of a conventional accumulator. FIG. 8 is a vertical 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: accumulator, 8: Compressor, 9: Condenser, 10: Evaporator, 11: Expansion mechanism, 12:
Multi-effect separator, 13: first expansion mechanism, 14: second expansion mechanism, 15: lubricating oil return passage, 16: third gas-liquid separation plate.
Claims (8)
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、密閉容器内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、前期気液分離器上部から下方に向かって流入す
る前記気液混相冷媒が衝突するように配置される第1及
び第2の気液分離板を設け、前記第1の気液分離板は前
記気液混相冷媒が前記気液分離器の内壁面との間に数mm
の隙間をもって配されており、第2の気液分離板は、前
記第1の気液分離板の下方に該第1の気液分離板と略平
行に前記気液分離器の内壁面と密着して配され、かつ、
その中央に、前記第1の気液分離板の径より小径又は同
等の開口を設けるとともに、前記蒸気出口管の開口端
を、前記第1の気液分離板の直下に設けたことを特徴と
する冷凍・冷房用気液分離器。1. An inlet part for introducing a gas-liquid mixed-phase refrigerant flowing from the outside into a closed container, and a steam outlet pipe having an open end in a container internal space for discharging steam in the closed container to the outside. , In a gas-liquid separator for refrigeration / cooling for separating a gas-liquid mixed phase refrigerant flowing into a closed container into a vapor and a liquid in the closed container, the gas-liquid flowing downward from the upper part of the gas-liquid separator in the previous period. First and second gas-liquid separating plates are provided so that the mixed-phase refrigerant collides with each other, and the first gas-liquid separating plate is provided between the gas-liquid mixed-phase refrigerant and the inner wall surface of the gas-liquid separator. Several mm
The second gas-liquid separation plate is disposed below the first gas-liquid separation plate and in close contact with the inner wall surface of the gas-liquid separator substantially parallel to the first gas-liquid separation plate. And arranged, and
In the center thereof, an opening having a diameter smaller than or equal to the diameter of the first gas-liquid separation plate is provided, and the opening end of the vapor outlet pipe is provided directly below the first gas-liquid separation plate. A gas-liquid separator for freezing and cooling.
気液分離板が配されており、これら第1乃至第3の気液
分離板は、前記気液混相冷媒の流れ方向に沿って間隔を
取り、前記気液混相冷媒が前記第1の気液分離板の板体
面を介してその外周より、前記第2の気液分離板の板体
面を介してその開口を通り、前記第3の気液分離板の板
体面を介してその外周へと、順次段階的に流れるように
配置されるとともに、前記蒸気出口管の開口端を、前記
第1又は第3の気液分離板の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. A third gas-liquid separation plate is disposed below the second gas-liquid separation plate, and the first to third gas-liquid separation plates are the gas-liquid mixed phase refrigerant. A space is provided along the flow direction, and the gas-liquid mixed phase refrigerant passes through the plate body surface of the first gas-liquid separation plate from its outer periphery to the opening through the plate body surface of the second gas-liquid separation plate. As described above, the third gas-liquid separating plate is arranged so as to sequentially flow in a stepwise manner through the plate surface of the third gas-liquid separating plate, and the opening end of the vapor outlet pipe is connected to the first or third gas The gas-liquid separator for refrigeration / cooling according to claim (1), which is opened immediately below the liquid separation plate.
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)又は第(2)項記載のいずれかの冷凍
・冷房用気液分離器。3. The first to second or the first to third gas-liquid separating plates have an integrated structure, and the first or second gas-liquid separating plate is integrated. A gas-liquid separator for either refrigeration or cooling.
くとも一つの気液分離板がぬれ性の良い材料にて作られ
ている特許請求の範囲第(1)又は第(2)項記載のい
ずれかの冷凍・冷房用気液分離器。4. At least one gas-liquid separation plate among the first to third gas-liquid separation plates is made of a material having a good wettability, according to claim (1) or (2). A gas-liquid separator for refrigeration / cooling according to any one of items.
た複数枚の板部材と、これらの板部材の相互間にはさま
れたぬれ性の良い材料とを含むものである特許請求の範
囲第(1)又は第(2)項記載のいずれかの冷凍・冷房
用気液分離器。5. The second gas-liquid separation plate includes a plurality of plate members having a large number of holes and a material having good wettability sandwiched between the plate members. The gas-liquid separator for refrigeration / cooling according to any one of claims (1) and (2).
囲第(5)項記載の冷凍・冷房用気液分離器。6. The gas-liquid separator for refrigeration / cooling according to claim 5, wherein the holes of the plate member are round holes.
特許請求の範囲第(5)項記載の冷凍・冷房用気液分離
器。7. The gas-liquid separator for refrigeration / cooling according to claim 5, wherein the plate member has a slit-shaped hole.
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. The plate member according to claim 5, wherein the surface of the plate member is coated with a material having good wettability.
A gas-liquid separator for refrigeration / cooling according to the item.
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 JPS63247571A (en) | 1988-10-14 |
JP2505194B2 true 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) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5520027B2 (en) * | 2009-12-11 | 2014-06-11 | 株式会社不二工機 | Accumulator and manufacturing method thereof |
JP2015034637A (en) * | 2011-11-22 | 2015-02-19 | パナソニック株式会社 | Gas-liquid separator and refrigeration cycle device |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS537715U (en) * | 1976-07-06 | 1978-01-23 | ||
JPS56139972U (en) * | 1980-03-21 | 1981-10-22 |
-
1987
- 1987-03-31 JP JP62079015A patent/JP2505194B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS63247571A (en) | 1988-10-14 |
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