JPH05322383A - Gas/liquid separator - Google Patents
Gas/liquid separatorInfo
- Publication number
- JPH05322383A JPH05322383A JP14838792A JP14838792A JPH05322383A JP H05322383 A JPH05322383 A JP H05322383A JP 14838792 A JP14838792 A JP 14838792A JP 14838792 A JP14838792 A JP 14838792A JP H05322383 A JPH05322383 A JP H05322383A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquid
- container
- liquid separator
- outlet pipe
- 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.)
- Pending
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
- F25B2400/02—Centrifugal separation of gas, liquid or oil
Landscapes
- Cyclones (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、気液分離器に関し、特
に複数の非共沸混合冷媒を用いた冷凍装置に好適な気液
分離器の構造に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-liquid separator, and more particularly to a structure of a gas-liquid separator suitable for a refrigeration system using a plurality of non-azeotropic mixed refrigerants.
【０００２】[0002]
【従来の技術】非共沸混合冷媒を用いた冷凍装置におい
て気液分離器は不可欠なものであり、例えば、図３に示
す３種類の混合冷媒を用いた冷凍装置では、気液分離器
（Ａ），（Ａ）が２個設けられている。そして、最初に
圧縮機（Ｂ）から吐出された３種類の混合冷媒を、凝縮
器（Ｃ）あるいはカスケードコンデンサ（Ｄ）を経るご
とに、気液分離器（Ａ）によって分離し、最後に最も低
沸点の冷媒だけを蒸発器（Ｅ）に流して、超低温冷熱を
生成可能としている。2. Description of the Related Art A gas-liquid separator is indispensable in a refrigeration system using a non-azeotropic mixed refrigerant. For example, in a refrigeration system using three types of mixed refrigerant shown in FIG. Two A) and (A) are provided. Then, first, the three types of mixed refrigerant discharged from the compressor (B) are separated by the gas-liquid separator (A) every time they pass through the condenser (C) or the cascade condenser (D), and finally the most mixed. Only low-boiling-point refrigerant is allowed to flow in the evaporator (E) to generate ultra-low temperature cold heat.
【０００３】こうした冷凍装置に設けられる気液分離器
は、とりわけ、気液分離効率が追求され、気液分離効率
のよさが、冷凍装置の能力を左右する。殊に、上記の如
き冷凍装置において、気液分離器に入ってくる流体の液
ガス混合割合は、液体７に対し気体３の割合であり、こ
れだけ液体含有率の多い流体を気液に分離するには、同
様の分離装置として知られる油分離器等と異なり、その
液封能力に極めて大きなものが要求される。ちなみに、
油分離器の場合は、液体は、気体９に対して１の割合で
ある。The gas-liquid separator provided in such a refrigeration system is particularly sought for gas-liquid separation efficiency, and the high efficiency of gas-liquid separation determines the capacity of the refrigeration system. In particular, in the refrigerating apparatus as described above, the liquid-gas mixing ratio of the fluid entering the gas-liquid separator is the ratio of the gas to the liquid of 7 and the liquid having such a high liquid content is separated into the gas and the liquid. In contrast to an oil separator or the like which is known as a similar separation device, a very large liquid sealing capacity is required. By the way,
In the case of an oil separator, the liquid is 1 to 9 gases.
【０００４】ところで、従来の気液分離器は、実開昭６
４−２５６７９号公報に記載されるように、遠心力を利
用して、気液分離をはかるものが一般的である。即ち、
気液分離器の本体容器が円筒状もしくは円錐状に形成さ
れ、その接線方向から流体をとり入れ、この流体を容器
内壁に沿って回転させ、その回転によって液体を容器内
壁に付着させ、気体を旋回流の中心に浮遊させて分離を
はかる方式である。By the way, the conventional gas-liquid separator is actually developed as follows.
As described in Japanese Unexamined Patent Publication No. 4-25679, it is common to use a centrifugal force to perform gas-liquid separation. That is,
The main container of the gas-liquid separator is formed in a cylindrical shape or a conical shape, takes in fluid from the tangential direction, rotates this fluid along the inner wall of the container, and the rotation causes the liquid to adhere to the inner wall of the container and swirls the gas. This is a method of floating in the center of the stream for separation.
【０００５】通常、分離された液体は容器下端の液体出
口管から排出され、気体は、容器上部に開口部を有する
気体出口管から排出されるようになっている。各出口管
は、通常の管体であり、例えば前記公報には気体出口管
として、容器内に立設された、筒状の管体（内筒）が示
されている。Usually, the separated liquid is discharged from a liquid outlet pipe at the lower end of the container, and the gas is discharged from a gas outlet pipe having an opening at the upper part of the container. Each of the outlet pipes is a normal pipe body, and for example, in the above-mentioned publication, a tubular pipe body (inner cylinder) erected in a container is shown as a gas outlet pipe.
【０００６】[0006]
【発明が解決しようとする課題】しかしながら、こうし
た従来の気液分離器において気液分離するとき、気体出
口管からは、未だ多くの液体が気体と共に排出されてお
り、気液分離効率が充分でないという問題があった。殊
に、流体中の液体量が少なくなると、充分に液封でき
ず、このため、気液分離効率が極端に悪化するという問
題があった。これを防ぐには、気液分離器そのものを充
分大きなものとすることが考えられるが、前記冷凍装置
に取り付ける場合、気液分離器はコンパクトさが要求さ
れ、大きくすることは、ほとんど不可能であった。However, when performing gas-liquid separation in such a conventional gas-liquid separator, a lot of liquid is still discharged together with the gas from the gas outlet pipe, and the gas-liquid separation efficiency is not sufficient. There was a problem. In particular, when the amount of liquid in the fluid becomes small, the liquid cannot be sufficiently sealed, which causes a problem that the gas-liquid separation efficiency is extremely deteriorated. To prevent this, it is conceivable to make the gas-liquid separator itself large enough, but when it is attached to the refrigeration system, the gas-liquid separator is required to be compact, and it is almost impossible to make it large. there were.
【０００７】本発明はかかる実状に鑑みて、コンパクト
であり、かつ充分な分離効率を備えた気液分離器を提供
することを目的とするものである。In view of such circumstances, it is an object of the present invention to provide a gas-liquid separator which is compact and has sufficient separation efficiency.
【０００８】[0008]
【課題を解決するための手段】即ち、上記目的に適合す
る本発明の特徴は、円筒状の容器（１）中央部接線方向
に流体入口管（５）を、容器（１）上端に気体出口
（７）を、そして容器（１）下端に液体出口管（８）を
夫々、取付け、容器（１）内壁に、前記流体入口管
（５）取着高さより僅か上方に位置して、下方に傾斜し
たじゃま板（６）を周設すると共に、前記気体出口管
（７）を、容器（１）上端を上下に貫通する管体（９）
により形成し、該管体（９）の下部に気体流出口（１
１）を設け、さらに該管体（９）の下端に、下方に頂部
を有する円錐状のツバ（１０）を固着し、該ツバ（１
０）の下端に細孔（１２）を開設して気液分離器を構成
したことである。That is, the feature of the present invention which meets the above-mentioned object is that a fluid inlet pipe (5) is provided tangentially to a central portion of a cylindrical container (1) and a gas outlet is provided at an upper end of the container (1). (7) and a liquid outlet pipe (8) at the lower end of the container (1), respectively, so that the liquid outlet pipe (8) is attached to the inner wall of the container (1) slightly above the attachment height of the fluid inlet pipe (5) and downward. A pipe body (9) which surrounds an inclined baffle plate (6) and vertically penetrates the gas outlet pipe (7) at the upper end of the container (1).
And the gas outlet (1
1) is provided, and further, a conical brim (10) having an apex below is fixed to the lower end of the tubular body (9), and the brim (1
That is, the gas-liquid separator is constructed by forming the pores (12) at the lower end of (0).
【０００９】[0009]
【作用】上記本発明気液分離器においては、流体入口管
（５）を通じて流入される流体が、じゃま板（６）を介
して下方に付勢され、同時に容器（１）内壁に沿って回
転して、下方への旋回流となり、この旋回の間に、流体
中の液体が遠心力により容器（１）内壁に付着し、容器
（１）下端の流体出口管（８）を経て容器（１）外に送
られる。そして、一方、流体中の気体は、この旋回中心
の負圧により、旋回中心に集められ、容器（１）内を上
昇し、一部はじゃま板（６）に当接し、さらに残りのほ
とんどは気体出口管（７）下端の円錐状ツバ（１０）に
当接して、その上昇速度が抑えられ、円錐状ツバ（１
０）を回り込んで、気体流出口（１１）から気体出口管
（７）に入り、容器（１）外へと上昇する。この間、気
体に残るわずかの液体は、気体がじゃま板（６）や、円
錐状ツバ（１０）に当接するとき、これらに付着して分
離され、さらに気体出口管（７）上昇中にも、該出口管
（７）内壁に付着して分離される。なお、円錐状ツバ
（１０）内壁や、気体出口管（７）内壁に付着した液滴
は、円錐状ツバ（１０）内部に集められた後、下端の細
孔（１２）を介して、容器（１）下端の液体出口管
（８）へと落下し、効率的に回収される。In the gas-liquid separator of the present invention described above, the fluid introduced through the fluid inlet pipe (5) is urged downward through the baffle plate (6) and simultaneously rotates along the inner wall of the container (1). Then, a downward swirling flow is generated, and during this swirling, the liquid in the fluid adheres to the inner wall of the container (1) due to centrifugal force, and passes through the fluid outlet pipe (8) at the lower end of the container (1) to the container (1 ) Will be sent out. On the other hand, the gas in the fluid is gathered at the swirl center due to the negative pressure at the swirl center, rises in the container (1), a part of the gas abuts on the baffle plate (6), and most of the rest remains. The rising speed is suppressed by contacting the conical brim (10) at the lower end of the gas outlet pipe (7), and the conical brim (1)
0), enters the gas outlet pipe (7) from the gas outlet (11), and rises to the outside of the container (1). During this time, a slight amount of the liquid remaining in the gas adheres to the baffle plate (6) and the conical brim (10) when the gas comes into contact with the baffle plate (6) and is separated, and even during the ascent of the gas outlet pipe (7), It adheres to the inner wall of the outlet pipe (7) and is separated. The droplets attached to the inner wall of the conical collar (10) and the inner wall of the gas outlet pipe (7) are collected inside the conical collar (10) and then passed through the pores (12) at the lower end of the container. (1) It drops into the liquid outlet pipe (8) at the lower end and is efficiently recovered.
【００１０】[0010]
【実施例】以下、本発明の実施例を図面にもとづき説明
する。図１は、本発明に係る気液分離器の一実施例を示
し、図１（イ）はその平面図、図１（ロ）はその側部断
面図である。これらの図において、（１）は気液分離器
の本体をなす容器であり、上部（２）、中央部（３）、
下部（４）よりなる。中央部（３）は円筒形状に形成さ
れていて、その外部には接線方向に沿って流体入口管
（５）が設けられ、内部には、この流体入口管（５）開
口部分よりわずか上方位置、好ましくは、上部（２）と
の境界位置あたりに、下方に傾斜したじゃま板（６）が
周設されている。また、上部（２）には、その上端に、
気体出口管（７）が固着され、下部（４）にはその下端
に液体出口管（８）が設けられている。Embodiments of the present invention will now be described with reference to the drawings. 1A and 1B show an embodiment of a gas-liquid separator according to the present invention. FIG. 1A is a plan view thereof and FIG. 1B is a side sectional view thereof. In these figures, (1) is a container that forms the body of the gas-liquid separator, and includes an upper part (2), a central part (3),
It consists of the lower part (4). The central portion (3) is formed in a cylindrical shape, a fluid inlet pipe (5) is provided on the outside along the tangential direction, and inside thereof is located slightly above the opening portion of the fluid inlet pipe (5). Preferably, a baffle plate (6) inclined downward is provided around the boundary position with the upper part (2). Also, on the upper part (2), at the upper end,
The gas outlet pipe (7) is fixed, and the lower portion (4) is provided with a liquid outlet pipe (8) at its lower end.
【００１１】ところで、上部（２）上端に設けられる気
体出口管（７）は、本発明の場合、上部（２）上端を貫
通して設けられており、その詳しい構造は、図２に示す
通りである。即ち、図２において、（９）は管体、（１
０）は該管体（９）下端に固着された円錐状のツバであ
り、該ツバ（１０）は、管体（９）下部を取り囲むよう
に、その頂部を下にして管体（９）下端に固着されてい
る。そして、管体（９）の下部側部に、所要大きさの気
体流出口（１１）が開設され、円錐状ツバ（１０）の下
端に、細孔（１２）が穿設されている。なお、前記容器
（１）に対しては、管体（９）の上部だけがわずかに容
器（１）上端より突出し、円錐状のツバ（１０）を含む
他の大部分が、容器（１）内に位置する如く固定され
る。このとき、円錐状ツバ（１０）の下端に位置する前
記細孔（１２）と、容器（１）下部（４）の液体出口管
（５）開口部分とが同一垂直線上に位置するように配設
されることが望ましい。By the way, in the present invention, the gas outlet pipe (7) provided at the upper end of the upper part (2) is provided so as to penetrate through the upper end of the upper part (2), and its detailed structure is as shown in FIG. Is. That is, in FIG. 2, (9) is a tubular body, and (1)
Reference numeral 0) is a conical brim fixed to the lower end of the tubular body (9), and the brim (10) is provided with the top thereof facing downward so as to surround the lower portion of the tubular body (9). It is fixed to the bottom edge. Then, a gas outlet (11) of a required size is opened on the lower side of the tubular body (9), and a small hole (12) is bored on the lower end of the conical flange (10). With respect to the container (1), only the upper part of the tubular body (9) slightly protrudes from the upper end of the container (1), and most of the other part including the conical flange (10) is the container (1). It is fixed so that it is located inside. At this time, the pores (12) located at the lower end of the conical collar (10) and the liquid outlet pipe (5) opening portion of the lower portion (4) of the container (1) are arranged on the same vertical line. It is desirable to be installed.
【００１２】次に以上の構成になる気液分離器の作用に
ついて説明する。流体入口管（５）を経て、容器（１）
中央部（３）に、その接線方向から流入した気液交合状
態の流体は、容器（１）内においてじゃま板（６）に当
接しつつ、中央部（３）内壁に沿って回転し、この結
果、容器（１）内には下方への旋回流が生じる。そし
て、この旋回流によって生ずる遠心力の作用により、旋
回流中に含まれる液体が、周囲の内壁に押し付けられ、
内壁に沿って下方へと流れ、下端の液体出口管（８）よ
り排出される。Next, the operation of the gas-liquid separator having the above structure will be described. Container (1) through fluid inlet pipe (5)
The fluid in the gas-liquid mixed state that has flowed into the central portion (3) from its tangential direction rotates along the inner wall of the central portion (3) while contacting the baffle plate (6) in the container (1), As a result, a downward swirl flow is generated in the container (1). Then, by the action of the centrifugal force generated by this swirling flow, the liquid contained in the swirling flow is pressed against the surrounding inner wall,
It flows downwards along the inner wall and is discharged from the liquid outlet pipe (8) at the lower end.
【００１３】さらに、一方では、上記旋回流により、旋
回中心部分に負圧が生じ、前記流体中、気体が、この負
圧のために、旋回中心部分を上昇する。この上昇する気
体について、わずかながらも、まだ液体が含まれている
ことは、前記した通りである。しかし、この気体は、こ
の後、容器（１）内を中央部（３）、上部（２）へと上
昇するにつれ、まず、その一部がじゃま板（６）に当接
し、次にそのほとんどが円錐状ツバ（１０）に当接する
等して、極端にその上昇速度を低下させる。そして、こ
の速度低下により、気体は、円錐状ツバ（１０）部分を
充分回り込んで、管体（９）の気体流出口（７）に至
り、管体（９）を上昇して、容器（１）外へと流出して
行く。Further, on the other hand, the swirl flow causes a negative pressure in the swirl center portion, and the gas in the fluid rises in the swirl center portion due to the negative pressure. As described above, the rising gas still contains a small amount of liquid. However, as this gas thereafter rises in the container (1) to the central part (3) and the upper part (2), first, a part of the gas abuts on the baffle plate (6), and then most of it. Comes into contact with the conical brim (10), etc., and its rising speed is extremely reduced. Then, due to this decrease in velocity, the gas sufficiently circulates around the conical brim (10) portion, reaches the gas outlet (7) of the pipe body (9), and ascends the pipe body (9) so that the container ( 1) It leaks out.
【００１４】こうして時間をかけて気体を上昇させる結
果、気体に含まれていた残りの液体は、そのほとんど
が、じゃま板（６）、円錐状ツバ（１０）さらには管体
（９）の内壁等に付着し、気体が容器（１）外に出たと
きは、ほとんど液体の含まれていなものとなる。なお、
容器（１）内において、上記の如く分離した液体は、じ
ゃま板（６）や円錐状ツバ（１０）下面に付着したもの
であれば、これらの傾斜に沿い、自と落下し、また、円
錐状ツバ（１０）上面や管体（９）内部に付着したもの
であれば、円錐状ツバ（１０）の内側に一旦集められた
後、細孔（１２）を通じて、直接液体出口管（８）へと
落下する。As a result of raising the gas over time, most of the remaining liquid contained in the gas is the baffle plate (6), the conical brim (10) and the inner wall of the tubular body (9). When it adheres to the like and the gas goes out of the container (1), it is almost free of liquid. In addition,
In the container (1), if the liquid separated as described above adheres to the lower surface of the baffle plate (6) or the conical brim (10), it will fall along with the inclination of the liquid and the cone. If it adheres to the upper surface of the brim (10) or the inside of the tubular body (9), it is once collected inside the conical brim (10) and then directly through the pores (12) to the liquid outlet pipe (8). Fall to.
【００１５】[0015]
【発明の効果】本発明は、以上説明したように、円筒状
の容器（１）の中央部接線方向に流体入口管（５）を、
容器（１）上端に気体出口（７）を、そして容器（１）
下端に液体出口管（８）を夫々取着すると共に、容器
（１）内壁には、前記流体入口管（５）取付け高さより
僅か上方に位置して、下方に傾斜したじゃま板（６）を
周設し、さらに、前記気体出口管（７）を、容器（１）
上端を上下に貫通する管体（９）と、該管体（９）下端
に固着された、下方に頂部を有する円錐状のツバ（１
０）とで構成し、管体（９）の下部に気体流出口（１
１）を開設する一方、前記円錐状のヅハ（１０）の下端
に細孔（１２）が開設して、気液分離器を構成したもの
であるから、気液混合した流体を旋回させて気液に分離
した後、容器（１）内を上昇する気体中に含まれる僅か
ながらの液体も、じゃま板（６）や円錐状ツバ（１０）
に付着させてほとんど完全に分離することができる。し
かも、こうして最後に分離した液体の一部は、円錐状ツ
バ（１０）の内部に貯溜した後、細孔（１２）を通じて
直接液体出口管（８）に落下させることができるため、
最後まで極めて効率的に、気液分離を遂行することがで
きる。従って、かかる気液分離器をコンパクトに構成し
ても、その気液分離効率は、充分、大きなものとなり、
前記混合冷媒を用いた冷凍装置に適用して、顕著な効果
を奏する。As described above, according to the present invention, the fluid inlet pipe (5) is provided in the tangential direction of the central portion of the cylindrical container (1).
Gas outlet (7) on top of container (1), and container (1)
The liquid outlet pipes (8) are attached to the lower ends, respectively, and the baffle plate (6), which is located slightly above the mounting height of the fluid inlet pipe (5) and is inclined downward, is attached to the inner wall of the container (1). The gas outlet pipe (7) is installed around the container (1).
A tubular body (9) that penetrates the upper end vertically and a conical collar (1) fixed to the lower end of the tubular body (9) and having a lower top.
0) and a gas outlet (1
While 1) is opened, the pores (12) are opened at the lower end of the conical duha (10) to form a gas-liquid separator, so that the gas-liquid mixed fluid is swirled. After being separated into gas and liquid, even a slight amount of liquid contained in the gas rising in the container (1) can be a baffle plate (6) or a conical brim (10).
And can be almost completely separated. Moreover, a part of the liquid finally separated in this way can be directly stored in the conical brim (10) and then dropped into the liquid outlet pipe (8) through the pores (12).
The gas-liquid separation can be performed extremely efficiently until the end. Therefore, even if such a gas-liquid separator is configured to be compact, the gas-liquid separation efficiency is sufficiently large,
When it is applied to a refrigeration system using the mixed refrigerant, a remarkable effect is obtained.
【図１】本発明気液分離器の説明図である。FIG. 1 is an explanatory view of a gas-liquid separator of the present invention.
【図２】本発明気液分離器の気体出口管部分の斜視図で
ある。FIG. 2 is a perspective view of a gas outlet pipe portion of the gas-liquid separator of the present invention.
【図３】気液分離器を備えた冷凍装置の配管構成図であ
る。FIG. 3 is a piping configuration diagram of a refrigeration apparatus including a gas-liquid separator.
（１） 容器 （５） 流体入口管 （６） じゃま板 （７） 気体出口管 （８） 液体出口管 （１０）円錐状ツバ （１２）細孔 (1) Container (5) Fluid inlet pipe (6) Baffle plate (7) Gas outlet pipe (8) Liquid outlet pipe (10) Conical flange (12) Pore
Claims (1)
使用される気液分離器であって、円筒状の容器（１）中
央部接線方向に流体入口管（５）を、容器（１）上端に
気体出口（７）を、そして容器（１）下端に液体出口管
（８）を夫々具備する一方、容器（１）内壁には、前記
流体入口管（５）取付け高さより僅か上方に位置して、
下方に傾斜したじゃま板（６）を周設してなり、前記気
体出口管（７）は、容器（１）上端を上下に貫通する管
体（９）より形成され、該管体（９）は、その下部に気
体流出口（１１）を有していると共に、その下端に、下
方に頂部を有する円錐状のツバ（１０）が固着され、該
ツバ（１０）の下端に細孔（１２）が開設されているこ
とを特徴とする気液分離器。1. A gas-liquid separator used in a refrigerating apparatus or the like using a non-azeotropic mixed refrigerant, comprising a cylindrical container (1), a fluid inlet pipe (5) in a tangential direction of a central part, and a container ( 1) A gas outlet (7) is provided at the upper end and a liquid outlet pipe (8) is provided at the lower end of the container (1), while the inner wall of the container (1) is slightly above the mounting height of the fluid inlet pipe (5). Located in
A baffle plate (6) inclined downward is provided around the gas outlet pipe (7), and the gas outlet pipe (7) is formed by a pipe body (9) vertically penetrating the upper end of the container (1). Has a gas outlet (11) in its lower part, and a cone-shaped brim (10) having a top portion at the bottom is fixed to the lower end thereof, and pores (12) are provided at the lower end of the brim (10). ) Is opened, a gas-liquid separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14838792A JPH05322383A (en) | 1992-05-15 | 1992-05-15 | Gas/liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14838792A JPH05322383A (en) | 1992-05-15 | 1992-05-15 | Gas/liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH05322383A true JPH05322383A (en) | 1993-12-07 |
Family
ID=15451638
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14838792A Pending JPH05322383A (en) | 1992-05-15 | 1992-05-15 | Gas/liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH05322383A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101135707B1 (en) * | 2011-10-14 | 2012-04-13 | (주)오선텍 | Gas-liquid separator of hydrogen generation device |
| CN102706047A (en) * | 2011-03-28 | 2012-10-03 | 株式会社电装 | Refrigerant distributor and refrigeration cycle device |
| KR101342157B1 (en) * | 2012-01-06 | 2013-12-13 | 지에스칼텍스 주식회사 | Gas-liquid separator for fuel cell having inclined operating condition |
| CN103477160A (en) * | 2011-03-28 | 2013-12-25 | 株式会社电装 | Pressure-reduction device and refrigeration cycle device |
| JP2014034069A (en) * | 2012-08-07 | 2014-02-24 | Disco Abrasive Syst Ltd | Exhaust duct of processing device |
| WO2020065712A1 (en) * | 2018-09-25 | 2020-04-02 | 東芝キヤリア株式会社 | Refrigeration cycle device |
| JPWO2021095116A1 (en) * | 2019-11-12 | 2021-05-20 | ||
| DE102021214236A1 (en) | 2021-12-13 | 2023-06-15 | Ekpo Fuel Cell Technologies Gmbh | liquid separator |
-
1992
- 1992-05-15 JP JP14838792A patent/JPH05322383A/en active Pending
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9239178B2 (en) | 2011-03-28 | 2016-01-19 | Denso Corporation | Refrigerant distributor and refrigeration cycle device |
| CN102706047A (en) * | 2011-03-28 | 2012-10-03 | 株式会社电装 | Refrigerant distributor and refrigeration cycle device |
| JP2012202652A (en) * | 2011-03-28 | 2012-10-22 | Denso Corp | Refrigerant distributor and refrigeration cycle |
| CN103477160A (en) * | 2011-03-28 | 2013-12-25 | 株式会社电装 | Pressure-reduction device and refrigeration cycle device |
| KR101135707B1 (en) * | 2011-10-14 | 2012-04-13 | (주)오선텍 | Gas-liquid separator of hydrogen generation device |
| KR101342157B1 (en) * | 2012-01-06 | 2013-12-13 | 지에스칼텍스 주식회사 | Gas-liquid separator for fuel cell having inclined operating condition |
| JP2014034069A (en) * | 2012-08-07 | 2014-02-24 | Disco Abrasive Syst Ltd | Exhaust duct of processing device |
| WO2020065712A1 (en) * | 2018-09-25 | 2020-04-02 | 東芝キヤリア株式会社 | Refrigeration cycle device |
| CN112771319A (en) * | 2018-09-25 | 2021-05-07 | 东芝开利株式会社 | Refrigeration cycle device |
| JPWO2020065712A1 (en) * | 2018-09-25 | 2021-08-30 | 東芝キヤリア株式会社 | Refrigeration cycle equipment |
| JPWO2021095116A1 (en) * | 2019-11-12 | 2021-05-20 | ||
| WO2021095116A1 (en) * | 2019-11-12 | 2021-05-20 | 三菱電機株式会社 | Refrigeration cycle device |
| DE102021214236A1 (en) | 2021-12-13 | 2023-06-15 | Ekpo Fuel Cell Technologies Gmbh | liquid separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4690759A (en) | Centrifugal and impingement oil separator | |
| CN103604258B (en) | A kind of discharge opeing type gas-liquid separator | |
| US4221577A (en) | Gas-liquid separator | |
| US5004043A (en) | Internal tubular falling film apparatus for the evaporation of liquids and for the absortion or degassing of solutions of two or more substances | |
| US2578568A (en) | Gas-liquid separator | |
| US4857197A (en) | Liquid separator with tangential drive fluid introduction | |
| CN2335686Y (en) | Cyclone filtering gas-liquid separator | |
| CN100531921C (en) | Cyclone liquid-gas separator | |
| FI943338A (en) | Gas-liquid separator | |
| US3581464A (en) | Method of and apparatus for separating a liquid from liquid vapor and dissolved gases | |
| US4290791A (en) | Gas-liquid separator | |
| JPH05322383A (en) | Gas/liquid separator | |
| US3212234A (en) | Separation method and apparatus | |
| US5242475A (en) | Oil separator and cone inlet diffuser | |
| JPH08159619A (en) | Oil separator and air compressor equipped with the separator | |
| CN109579379A (en) | Air regulator and its gas-liquid separator | |
| JP3593594B2 (en) | Gas-liquid separator | |
| JPH0618127A (en) | Oil separator | |
| JP2001121036A (en) | Centrifugal separator | |
| JPH11248296A (en) | Oil separator | |
| JPH08110128A (en) | Oil separator | |
| JP2965251B1 (en) | Cyclone type gas-liquid separator | |
| US6589322B2 (en) | Oil seal liquid separator | |
| JP2002200402A (en) | Gas-liquid separator and gas-liquid separating apparatus provided therewith | |
| JPH08261603A (en) | Gas-liquid separator |