JPH1043293A - Device for removing bubble in liquid - Google Patents

Device for removing bubble in liquid

Info

Publication number
JPH1043293A
JPH1043293A JP8210311A JP21031196A JPH1043293A JP H1043293 A JPH1043293 A JP H1043293A JP 8210311 A JP8210311 A JP 8210311A JP 21031196 A JP21031196 A JP 21031196A JP H1043293 A JPH1043293 A JP H1043293A
Authority
JP
Japan
Prior art keywords
liquid
bubbles
filter
space
blood
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
Application number
JP8210311A
Other languages
Japanese (ja)
Inventor
Hiroshi Maruya
拓 丸屋
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.)
SENKO IKA KOGYO KK
Senko Medical Instrument Manufacturing Co Ltd
Original Assignee
SENKO IKA KOGYO KK
Senko Medical Instrument Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SENKO IKA KOGYO KK, Senko Medical Instrument Manufacturing Co Ltd filed Critical SENKO IKA KOGYO KK
Priority to JP8210311A priority Critical patent/JPH1043293A/en
Publication of JPH1043293A publication Critical patent/JPH1043293A/en
Pending legal-status Critical Current

Links

Landscapes

  • External Artificial Organs (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

PROBLEM TO BE SOLVED: To reduce pressure loss and improve the bubble removing effect by providing a cyclone part in a vessel main body to make a liquid to be processed a swirl flow to be gas-liquid separated. SOLUTION: When blood to be processed is introduced in a liquid inflow space 15 from a liquid inlet of a device for removing bubbles in a liquid used with an artificial heart device or the like, the liquid to be processed occupies the total capacity of the liquid inflow space 15. The liquid is made into a swirl flow by a cyclone 19. That is, rotary momentum is given to the blood to be processed flowing from the liquid inlet 18 in the process of moving along the surface of a lower annular partition wall 17 to form a continuous swirl flow. While the liquid inflow space 15 is turned, it is moved upward. In this process, blood and bubbles which have different specific gravities are separated from each other by the action of centrifugal force, and the bubbles are collected in the central part to be discharged from a gas outlet 12 and removed. The blood from which bubbles are removed is discharged from an outflow opening 13.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、人工心肺装置、人
工腎臓装置、血球成分と血漿成分の分離装置等の体外循
環用血液、または、人工腎臓装置における透析液回路中
を流れる透析液等の液体より気泡を除去する液体中気泡
除去装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to blood for extracorporeal circulation such as an artificial heart-lung machine, an artificial kidney apparatus, an apparatus for separating blood cells and plasma components, or a dialysate flowing through a dialysate circuit in an artificial kidney apparatus. The present invention relates to an apparatus for removing bubbles in liquid that removes bubbles from liquid.

【0002】[0002]

【従来の技術】液体中気泡除去装置としては、例えば特
開昭59−228849公報、特公昭61−44031
公報に示すように、濾過方式、滞留方式、濾過方式と滞
留方式の併用方式がある。
2. Description of the Related Art As an apparatus for removing air bubbles in a liquid, for example, Japanese Patent Application Laid-Open No. 59-228849 and Japanese Patent Publication No. 61-44031 are known.
As shown in the gazette, there are a filtration system, a residence system, and a combination system of the filtration system and the residence system.

【0003】従来の液体中気泡除去装置の一例には、図
4に示すように、容器本体1に液入口2、液出口3、気
体出口4が配され、内部に濾過体5が上部空間6と下部
空間7を画すよう配されている。濾過体5は円錐形状と
され、上部に上部空間6と下部空間7を連通する連通孔
8が形成される遮断板9が配されている。この液体中気
泡除去装置では、液入口2から液体が旋回流を形成して
容器本体1に流入し、旋回流の流速が大なる外周部で液
体中の気泡を積極的に遠心分離した後、流速が遅くなる
中央部側で既に遠心分離されている気泡に大きな浮力上
昇作用を与えて気泡を分離し、さらに残った気泡を濾過
体5で濾過することで気泡除去をおこない、集まった気
泡を気体出口4から排出して、気泡除去した液体を液出
口3から送出していた。
As one example of a conventional apparatus for removing bubbles in liquid, as shown in FIG. 4, a liquid inlet 2, a liquid outlet 3, and a gas outlet 4 are arranged in a container body 1, and a filter 5 is provided inside the upper space 6 as shown in FIG. And a lower space 7. The filter 5 has a conical shape, and is provided with a blocking plate 9 having a communication hole 8 formed at an upper portion thereof for communicating the upper space 6 and the lower space 7. In this device for removing bubbles in liquid, the liquid forms a swirling flow from the liquid inlet 2 and flows into the container body 1, and after the bubbles in the liquid are positively centrifuged at the outer periphery where the flow velocity of the swirling flow is large, At the center where the flow velocity is slow, a large buoyancy is raised to the air bubbles that have already been centrifuged to separate the air bubbles, and the remaining air bubbles are filtered by the filter 5 to remove the air bubbles, and the collected air bubbles are removed. The liquid from which the gas was removed from the gas outlet 4 and from which bubbles were removed was sent out from the liquid outlet 3.

【0004】[0004]

【発明が解決しようとする課題】しかし、集まった気泡
が多くなってしまうと上部空間6に渦流が形成され、遮
断板9や濾過体5の下方の下部空間7に気体が侵入して
しまい、液出口3に吸引される。下部空間7に気体が溜
まってしまうと連通孔8から上部空間6への排出がうま
くいかず、気泡除去の効率が低下するという可能性があ
った。また、濾過を行う際に、圧力損失が生じていた。
However, if the number of collected bubbles increases, a vortex is formed in the upper space 6 and gas enters the lower space 7 below the blocking plate 9 and the filter 5, The liquid is sucked into the liquid outlet 3. If the gas accumulates in the lower space 7, the gas cannot be discharged from the communication hole 8 to the upper space 6, and the efficiency of air bubble removal may be reduced. In addition, a pressure loss occurred during the filtration.

【0005】本発明は、上記の事情に鑑みてなされたも
ので、以下の目的を達成しようとするものである。 流体が旋回流を形成する遠心分離による気泡除去効果
を向上すること。 流体の形成する旋回流の中心から液出口を遠ざけて気
泡の浮力上昇作用による気泡除去効果を向上すること。 旋回流による遠心作用を利用して濾過を行い圧力損失
の低下を図ること。 液体の流速の低速化を図り、滞留による気泡除去の効
果を向上すること。 分離された気泡の停留する部分から液出口を離し、液
出口への気泡の侵入を低減すること。
The present invention has been made in view of the above circumstances, and aims to achieve the following objects. To improve the air bubble removal effect by centrifugal separation in which a fluid forms a swirling flow. To improve the bubble removal effect by increasing the buoyancy of bubbles by moving the liquid outlet away from the center of the swirling flow formed by the fluid. Filtration using centrifugal action by swirling flow to reduce pressure loss. To reduce the flow velocity of the liquid and improve the effect of removing bubbles by staying. Separating the liquid outlet from the portion where the separated bubbles stay, and reducing the intrusion of bubbles into the liquid outlet.

【0006】[0006]

【課題を解決するための手段】容器本体と、容器本体内
に設けられ液体流入空間と液体流出空間に画する濾過体
と、容器本体に液体流入空間と連通するように設けられ
る液入口と、容器本体に配され被処理液体を旋回流とし
て気液分離をおこなうサイクロン部と、容器本体に液体
流出空間と連通するように設けられ濾過体を通過した処
理液体を送出する液出口と、液体流入空間の上部に対し
連通状態に配される気体出口とを備え、濾過体が容器本
体の内部に立設される円筒形状とされ、濾過体の内部に
液体流入空間が配され、濾過体の外側に液体流出空間が
配される。液入口と液出口とが本体容器下部の同一高さ
に配され、液入口が液体流出空間を貫通して液体流入空
間に接続される。サイクロン部は、濾過体下部に配さ
れ、液入口が接続される状態で容器本体に接続され、流
体の流体流出空間への進入を阻止する円環状隔壁が配さ
れる。サイクロン部に、被処理液体を旋回流として気液
分離をおこなうひねり板が配される。濾過体は孔径30
〜200μmの多孔質体からなり、濾過体の上部と容器
本体内側の上部の間に間隙が配される。容器本体の上部
に内方に傾斜形状のテーパ部が配され気体出口に連通さ
れる。
A container body, a filter provided in the container body to define a liquid inflow space and a liquid outflow space, a liquid inlet provided in the container body so as to communicate with the liquid inflow space, A cyclone section disposed in the container body to perform gas-liquid separation by using the liquid to be processed as a swirling flow; a liquid outlet provided in the container body so as to communicate with the liquid outflow space; A gas outlet provided in communication with the upper part of the space, a filter having a cylindrical shape standing upright inside the container body, a liquid inflow space disposed inside the filter, and an outside of the filter A liquid outflow space is disposed at the bottom. The liquid inlet and the liquid outlet are arranged at the same height below the main body container, and the liquid inlet penetrates the liquid outflow space and is connected to the liquid inflow space. The cyclone portion is disposed below the filter, connected to the container body with the liquid inlet connected thereto, and provided with an annular partition for preventing fluid from entering the fluid outflow space. A twist plate that performs gas-liquid separation using the liquid to be processed as a swirling flow is disposed in the cyclone unit. Filter has a pore size of 30
It is made of a porous material having a thickness of about 200 μm, and a gap is provided between an upper portion of the filter and an upper portion inside the container body. An inclined tapered portion is disposed inward at an upper portion of the container body and communicates with the gas outlet.

【0007】[0007]

【発明の実施の形態】以下、本発明に係る液体中気泡除
去装置の第1実施形態を、図面に基づいて説明する。図
1及び図2において、符号11は容器本体、12は気体
出口、13は液出口、14は濾過体、15は液体流入空
間、16は液体流出空間、17は下部円環状隔壁(円環
状隔壁)、18は液入口、19はサイクロン部である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a first embodiment of a device for removing bubbles in liquid according to the present invention will be described with reference to the drawings. 1 and 2, reference numeral 11 denotes a container body, 12 denotes a gas outlet, 13 denotes a liquid outlet, 14 denotes a filter, 15 denotes a liquid inflow space, 16 denotes a liquid outflow space, and 17 denotes a lower annular partition (annular partition). ) And 18 are a liquid inlet and 19 is a cyclone part.

【0008】容器本体11は円筒形状とされ、上部に内
方に傾斜形状のテーパ部11aが配され内部に気泡溜ま
り11bを形成し、該テーパ部11aの中心に気体出口
12が位置され、容器本体11下部の側面に液出口13
が位置される。容器本体11の内部には、円筒形状の濾
過体14が容器本体11の中心軸と同軸状に配され、濾
過体14の内側空間が液体流入空間15とされ、濾過体
14の外側空間が液体流出空間16とされる。濾過体1
4は例えば孔径30〜200μmの多孔質体により構成
される。
The container body 11 has a cylindrical shape, and a tapered portion 11a having an inclined shape is disposed inward at an upper portion thereof to form a bubble reservoir 11b therein. A gas outlet 12 is located at the center of the tapered portion 11a. A liquid outlet 13 is provided on the lower side of the main body 11.
Is located. Inside the container body 11, a cylindrical filter body 14 is arranged coaxially with the central axis of the container body 11, the inner space of the filter body 14 is a liquid inflow space 15, and the outer space of the filter body 14 is liquid. Outflow space 16 is provided. Filter 1
4 is made of, for example, a porous body having a pore diameter of 30 to 200 μm.

【0009】濾過体14の下部には、容器本体11の底
面に接続される下部円環状隔壁17が配され、濾過体1
4の上部には、接続部材14aにより下部円環状隔壁1
7と接続された上部円環状隔壁14bが配される。下部
円環状隔壁17には液体流出空間16を貫いて外部に連
通状態とされる液入口18が下部円環状隔壁17の接線
方向に接続され、該液入口18、下部円環状隔壁17は
サイクロン部19を形成している。上部円環状隔壁14
bはテーパ部11aの近傍に位置し、濾過体14とテー
パ部11aの間に間隙Gを形成している。
A lower annular partition 17 connected to the bottom surface of the container body 11 is disposed below the filter 14,
4 is connected to the lower annular partition 1 by a connecting member 14a.
7 is provided. A liquid inlet 18 which is communicated to the outside through the liquid outflow space 16 is connected to the lower annular partition 17 in a tangential direction of the lower annular partition 17, and the liquid inlet 18 and the lower annular partition 17 are connected to a cyclone portion. 19 are formed. Upper annular partition 14
b is located near the tapered portion 11a, and forms a gap G between the filter 14 and the tapered portion 11a.

【0010】このような液体中気泡除去装置にあって
は、例えば人工心臓装置の人工肺と人体の大動脈を結ぶ
血回路の途中に取り付けられ、気体出口12に気体を排
出する弁を装着して使用される。
In such an apparatus for removing bubbles in liquid, for example, a valve for discharging gas from the gas outlet 12 is attached to a part of the blood circuit connecting the artificial lung of the artificial heart device and the aorta of the human body. used.

【0011】被処理血液が液入口18から液体流入空間
15に導入されると、被処理血液は液体流入空間15の
全容積を占めて、図2に示す矢印のように、サイクロン
部19によって旋回流となる。ここで、液入口18から
侵入した被処理血液には、下部円環状隔壁17の面に沿
って移動していく過程で、回転運動量が与えられること
で、連続した旋回流が形成される。
When the blood to be processed is introduced from the liquid inlet 18 into the liquid inflow space 15, the blood to be processed occupies the entire volume of the liquid inflow space 15 and is swirled by the cyclone 19 as shown by an arrow in FIG. It becomes a flow. Here, a continuous swirling flow is formed by applying rotational momentum to the blood to be treated that has entered through the liquid inlet 18 while moving along the surface of the lower annular partition wall 17.

【0012】図1に示す矢印のように旋回流となった被
処理血液は、液体流入空間15内部を旋回しながら上方
に移動してゆく。ここで、旋回流の流速が大なる外周部
では、比重の異なる血液と気泡に大なる遠心力が作用す
ることから、血液中の気泡が積極的に遠心分離され中央
部分に移行してゆく。このように遠心分離された気泡は
次第に流速を低下して中央部分に移行するに従い大きな
浮力作用が作用し上方に移動してゆく。この際、血液は
遠心作用により加圧された状態で濾過体14を通過して
液体流出空間16に流入し、液出口13から流出する。
液体流出空間16では、血液の流速が液体流入空間15
内部より緩やかになっており、血液が液体流出空間16
内部を下降してゆく間に、血液中に残存する気泡が浮力
作用により上方に移動してゆく。
The blood to be processed, which has been swirled as indicated by the arrow shown in FIG. 1, moves upward while swirling inside the liquid inflow space 15. Here, in the outer peripheral portion where the flow velocity of the swirling flow is large, since a large centrifugal force acts on blood and bubbles having different specific gravities, the bubbles in the blood are positively centrifuged and moved to the central portion. The bubbles centrifuged in this way gradually decrease in flow velocity and move upward due to a large buoyancy effect as they move toward the center. At this time, the blood flows into the liquid outflow space 16 through the filter 14 in a state of being pressurized by the centrifugal action, and flows out of the liquid outlet 13.
In the liquid outflow space 16, the blood flow velocity is
It is gentler than the inside, and blood
While descending inside, the air bubbles remaining in the blood move upward by buoyancy.

【0013】液体流入空間15の上部に移動した気泡は
気泡溜まり11bに集まり、液体流出空間16の上部に
移動して間隙Gを経て気泡溜まり11bに到達した気泡
とともに、一定量集まる度に装着された弁を開き気体出
口12から除去される。
The bubbles that have moved to the upper part of the liquid inflow space 15 collect in the bubble reservoir 11b, move to the upper part of the liquid outflow space 16, and are attached to the bubble reservoir 11b via the gap G every time a certain amount of bubbles are collected. The valve is opened and removed from the gas outlet 12.

【0014】以下、本発明に係る液体中気泡除去装置の
第2実施形態を、図面に基づいて説明する。図3におい
て、符号21は容器本体、22は気体出口、23は液出
口、24は濾過体、25は液体流入空間、26は液体流
出空間、27は下部円環状隔壁(円環状隔壁)、28は
液入口、29はサイクロン部である。
Hereinafter, a second embodiment of the apparatus for removing bubbles in liquid according to the present invention will be described with reference to the drawings. 3, reference numeral 21 denotes a container body, 22 denotes a gas outlet, 23 denotes a liquid outlet, 24 denotes a filter, 25 denotes a liquid inflow space, 26 denotes a liquid outflow space, 27 denotes a lower annular partition (annular partition), 28 Is a liquid inlet, and 29 is a cyclone portion.

【0015】容器本体21は円筒形状とされ、上部に内
方に傾斜形状のテーパ部21aが配され内部に気泡溜ま
り21bを形成し、該テーパ部21aの中心に気体出口
22が位置され、容器本体21の下部側面に液出口23
が配される。容器本体21の内部には、円筒形状の濾過
体24が容器本体21の中心軸と同軸状に配され、濾過
体24の内側空間が液体流入空間25とされ、濾過体2
4の外側空間が液体流出空間26とされる。濾過体24
は例えば孔径30〜200μmの多孔質体により構成さ
れる。
The container body 21 has a cylindrical shape, and a tapered portion 21a having an inclined shape is disposed inward at an upper portion thereof to form a bubble reservoir 21b therein. A gas outlet 22 is located at the center of the tapered portion 21a. A liquid outlet 23 is provided on the lower side surface of the main body 21.
Is arranged. Inside the container body 21, a cylindrical filter body 24 is disposed coaxially with the central axis of the container body 21, the inner space of the filter body 24 is defined as a liquid inflow space 25, and the filter body 2
The space outside 4 is a liquid outflow space 26. Filter body 24
Is made of a porous material having a pore diameter of 30 to 200 μm, for example.

【0016】濾過体24の下部には、容器本体21の底
面に接続される下部円環状隔壁27が配され、濾過体2
4の上部には、接続部材24aにより下部円環状隔壁2
7と接続された上部円環状隔壁24bが配される。容器
本体21の底面には下方から外部に連通状態とされる液
入口28が接続され、該液入口28には、下部円環状隔
壁27に接続されるよう内方に傾斜形状のテーパ部27
aが配される。下部円環状隔壁27とテーパ部27a、
液入口28はサイクロン部29を形成し、サイクロン部
29の内部には、被処理液体を旋回流として気液分離を
おこなう例えば2枚のひねり板29aが、互いに角度を
もって配される。上部円環状隔壁24bはテーパ部21
aの近傍に位置し、濾過体24とテーパ部21aの間に
間隙Gを形成している。
A lower annular partition wall 27 connected to the bottom surface of the container body 21 is disposed below the filter body 24.
4 is connected to the lower annular partition 2 by a connecting member 24a.
7 is provided. The bottom surface of the container body 21 is connected to a liquid inlet 28 which is in communication with the outside from below. The liquid inlet 28 has an inwardly tapered portion 27 which is connected to the lower annular partition wall 27.
a is arranged. A lower annular partition wall 27 and a tapered portion 27a,
The liquid inlet 28 forms a cyclone portion 29, and inside the cyclone portion 29, for example, two twist plates 29a for performing gas-liquid separation using a liquid to be processed as a swirling flow are arranged at an angle to each other. The upper annular partition 24b has a tapered portion 21.
a gap G is formed between the filter body 24 and the tapered portion 21a.

【0017】このような液体中気泡除去装置にあって
は、例えば人工心臓装置の人工肺と人体の大動脈を結ぶ
血回路の途中に取り付けられ、気体出口22に気体を排
出する弁を装着して使用される。
In such a device for removing air bubbles in a liquid, for example, a valve for discharging gas at the gas outlet 22 is provided which is attached in the middle of a blood circuit connecting the artificial lung of the artificial heart device and the aorta of the human body. used.

【0018】被処理血液が液入口28から液体流入空間
25に導入されると、被処理血液は液体流入空間25の
全容積を占めて、図3に示す矢印のように、サイクロン
部29によって旋回流となる。これは、液入口28から
侵入した被処理血液がひねり板29aの面に沿って移動
していく過程で、回転運動量が与えられることで、連続
した旋回流が形成される。
When the blood to be processed is introduced from the liquid inlet 28 into the liquid inflow space 25, the blood to be processed occupies the entire volume of the liquid inflow space 25 and is swirled by the cyclone 29 as shown by the arrow in FIG. It becomes a flow. This is because a continuous swirling flow is formed by applying a rotational momentum in the process in which the blood to be treated that has entered from the liquid inlet 28 moves along the surface of the twist plate 29a.

【0019】旋回流となった被処理血液は、液体流入空
間25内部を旋回しながら上方に移動してゆく。ここ
で、旋回流の流速が大なる外周部では、比重の異なる血
液と気泡に大なる遠心力が作用することから、血液中の
気泡が積極的に遠心分離され中央部分に移行してゆく。
このように遠心分離された気泡は次第に流速を低下して
中央部分に移行するに従い大きな浮力作用が作用し上方
に移動してゆく。この際、血液は遠心作用により加圧さ
れた状態で濾過体24を通過して液体流出空間26に流
入し、液出口23から流出する。液体流出空間26で
は、血液の流速が液体流入空間25内部より緩やかにな
っており、血液が液体流出空間26内部を下降してゆく
間に、血液中に残存する気泡が浮力作用により上方に移
動してゆく。
The blood to be processed, which has been swirled, moves upward while swirling inside the liquid inflow space 25. Here, in the outer peripheral portion where the flow velocity of the swirling flow is large, since a large centrifugal force acts on blood and bubbles having different specific gravities, the bubbles in the blood are positively centrifuged and moved to the central portion.
The bubbles centrifuged in this way gradually decrease in flow velocity and move upward due to a large buoyancy effect as they move toward the center. At this time, the blood flows into the liquid outflow space 26 through the filter body 24 while being pressurized by the centrifugal action, and flows out from the liquid outlet 23. In the liquid outflow space 26, the flow velocity of the blood is slower than in the liquid inflow space 25, and while the blood descends in the liquid outflow space 26, the air bubbles remaining in the blood move upward by buoyancy. I will do it.

【0020】液体流入空間25の上部に移動した気泡は
気泡溜まり21bに集まり、液体流出空間26の上部に
移動して間隙Gを経て気泡溜まり21bに到達した気泡
とともに、一定量集まる度に装着された弁を開き気体出
口22から除去される。
The bubbles that have moved to the upper part of the liquid inflow space 25 collect in the bubble reservoir 21b, move to the upper part of the liquid outflow space 26, and are attached to the bubble reservoir 21b via the gap G every time a certain amount of bubbles are collected. The valve is opened and removed from the gas outlet 22.

【0021】[0021]

【発明の効果】本発明の液体中気泡除去装置によれば、
以下の効果を奏する。 (1)被処理液体が旋回流を形成し液体が分離され移動
してくる旋回流の外側に液体流出空間を設けたので、遠
心分離による気泡除去効果を向上することができる。 (2)液出口を気泡濃度の低くなる旋回流の外側に設
け、かつ、気泡の浮力上昇作用により気泡が上昇して気
泡濃度の低くなる下側に設けたので、気泡除去効果を向
上することができる。 (3)被処理液体が旋回流を形成し液体が分離され移動
してくる旋回流の外側に濾過体を設けたので、旋回流に
よる遠心作用を利用して濾過を行い圧力損失の低下を図
ることができる。 (4)液体流出空間を液体流入空間の外側に設けたの
で、液体流出空間の液体の流速が緩やかになり、滞留に
よる気泡除去の効果を向上することができる。 (5)液出口を容器本体の下部に設けたので、分離され
た気泡の停留する部分から液出口を離し、液出口への気
泡の侵入を低減することができる。
According to the apparatus for removing bubbles in liquid of the present invention,
The following effects are obtained. (1) Since the liquid to be processed forms a swirl flow and the liquid outflow space is provided outside the swirl flow from which the liquid is separated and moved, the bubble removal effect by centrifugal separation can be improved. (2) Since the liquid outlet is provided outside the swirling flow where the bubble concentration becomes low, and the liquid outlet is provided below the bubble where the bubble rises due to the action of increasing the buoyancy of the bubble and the bubble concentration becomes low, the bubble removing effect is improved. Can be. (3) Since the liquid to be processed forms a swirl flow and the filter is provided outside the swirl flow from which the liquid is separated and moves, the filtration is performed by utilizing the centrifugal action of the swirl flow to reduce the pressure loss. be able to. (4) Since the liquid outflow space is provided outside the liquid inflow space, the flow velocity of the liquid in the liquid outflow space becomes gentle, and the effect of removing air bubbles due to stagnation can be improved. (5) Since the liquid outlet is provided at the lower part of the container body, the liquid outlet is separated from the portion where the separated bubbles stay, so that the intrusion of bubbles into the liquid outlet can be reduced.

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

【図1】 本発明に係る液体中気泡除去装置の第1実施
形態を示す一部の記載を省略した正断面図である。
FIG. 1 is a front cross-sectional view of a first embodiment of a device for removing bubbles in liquid according to the present invention, with a part of the description omitted;

【図2】 図1の液体中気泡除去装置の側断面図であ
る。
FIG. 2 is a side sectional view of the apparatus for removing bubbles from liquid in liquid of FIG. 1;

【図3】 本発明に係る液体中気泡除去装置の第2実施
形態を示す一部の記載を省略した正断面図である。
FIG. 3 is a front cross-sectional view of a second embodiment of the apparatus for removing bubbles in liquid according to the present invention, in which some descriptions are omitted.

【図4】 従来の液体中気泡除去装置の例を示す一部の
記載を省略した正断面図である。
FIG. 4 is a front cross-sectional view of an example of a conventional apparatus for removing bubbles in liquid, in which some descriptions are omitted.

【符号の説明】[Explanation of symbols]

1…容器本体,2…液入口,3…液出口,4…気体出
口,5…濾過体,6…上部空間,7…下部空間,8…連
通孔,9…遮断板,11…容器本体,11a…テーパ
部,11b…気泡溜まり,12…気体出口,13…液出
口,14…濾過体,14a…接続部材,14b…上部円
環状隔壁,15…液体流入空間,16…液体流出空間,
17…下部円環状隔壁(円環状隔壁),18…液入口,
19…サイクロン部,21…容器本体,21a…テーパ
部,21b…気泡溜まり,22…気体出口,23…液出
口,24…濾過体,24a…接続部材,24b…上部円
環状隔壁,25…液体流入空間,26…液体流出空間,
27…下部円環状隔壁(円環状隔壁),27a…テーパ
部,28…液入口,29…サイクロン部,29a…ひね
り板,G…間隙
DESCRIPTION OF SYMBOLS 1 ... Container main body, 2 ... Liquid inlet, 3 ... Liquid outlet, 4 ... Gas outlet, 5 ... Filter body, 6 ... Upper space, 7 ... Lower space, 8 ... Communication hole, 9 ... Blocking plate, 11 ... Container main body, 11a: tapered portion, 11b: bubble reservoir, 12: gas outlet, 13: liquid outlet, 14: filter, 14a ... connecting member, 14b: upper annular partition wall, 15: liquid inflow space, 16: liquid outflow space,
17: lower annular partition (annular partition), 18: liquid inlet,
19 cyclone part, 21 container body, 21a taper part, 21b bubble reservoir, 22 gas outlet, 23 liquid outlet, 24 filter body, 24a connecting member, 24b upper annular partition, 25 liquid Inflow space, 26 ... liquid outflow space,
27: lower annular partition (annular partition), 27a: tapered portion, 28: liquid inlet, 29: cyclone portion, 29a: twist plate, G: gap

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 容器本体(11,21)と、容器本体内
に設けられ液体流入空間(15,25)と液体流出空間
(16,26)に画する濾過体(14,24)と、容器
本体に液体流入空間と連通するように設けられる液入口
(18,28)と、容器本体に配され被処理液体を旋回
流として気液分離をおこなうサイクロン部(19,2
9)と、容器本体に液体流出空間と連通するように設け
られ濾過体を通過した処理液体を送出する液出口(1
3,23)と、液体流入空間の上部に対し連通状態に配
される気体出口(12,22)とを備え、濾過体が容器
本体の内部に立設される円筒形状とされ、濾過体の内部
に液体流入空間が配され、濾過体の外側に液体流出空間
が配されることを特徴とする液体中気泡除去装置。
1. A container body (11, 21), a filter (14, 24) provided in the container body and defining a liquid inflow space (15, 25) and a liquid outflow space (16, 26), and a container. A liquid inlet (18, 28) provided in the main body so as to communicate with the liquid inflow space; and a cyclone section (19, 2) arranged in the container main body and performing gas-liquid separation using the liquid to be treated as a swirling flow.
9) and a liquid outlet (1) which is provided in the container body so as to communicate with the liquid outflow space and which sends out the processing liquid passing through the filter.
3, 23) and a gas outlet (12, 22) arranged in communication with the upper part of the liquid inflow space, and the filter is formed in a cylindrical shape standing upright inside the container body. An apparatus for removing bubbles in a liquid, wherein a liquid inflow space is provided inside and a liquid outflow space is provided outside the filter.
【請求項2】 液入口(18,28)が本体容器(1
1,21)の下部に配され、液出口(13,23)が本
体容器の下部に配されることを特徴とする請求項1記載
の液体中気泡除去装置。
2. The liquid inlet (18, 28) is provided with a main container (1).
The apparatus for removing bubbles in a liquid according to claim 1, wherein the liquid outlet (13, 23) is disposed at a lower portion of the main body container.
【請求項3】 サイクロン部(19,29)に、液体の
液体流出空間(16,26)への進入を阻止する円環状
隔壁(17,27)が配されることを特徴とする請求項
1または2記載の液体中気泡除去装置。
3. An annular partition (17, 27) for preventing liquid from entering the liquid outflow space (16, 26) is disposed in the cyclone portion (19, 29). Or the apparatus for removing bubbles in liquid according to 2.
【請求項4】 サイクロン部(29)に、被処理液体を
旋回流として気液分離をおこなうひねり板(29a)が
配されることを特徴とする請求項1から3のいずれか記
載の液体中気泡除去装置。
4. A liquid in a liquid according to claim 1, wherein a twist plate (29a) for performing gas-liquid separation by using a liquid to be treated as a swirling flow is disposed in the cyclone section (29). Bubble removal device.
【請求項5】 濾過体(14,24)は孔径30〜20
0μmの多孔質体からなることを特徴とする請求項1か
ら4のいずれか記載の液体中気泡除去装置。
5. The filter (14, 24) has a pore size of 30 to 20.
The apparatus for removing bubbles in a liquid according to any one of claims 1 to 4, wherein the apparatus is made of a porous material having a thickness of 0 µm.
【請求項6】 液入口(18)と液出口(13)とが同
一高さに配されることを特徴とする請求項1、2、3、
または5のいずれか記載の液体中気泡除去装置。
6. The liquid inlet (18) and the liquid outlet (13) are arranged at the same height.
6. The apparatus for removing bubbles in a liquid according to any one of the above items 5.
【請求項7】 濾過体(14,24)の上部と容器本体
(11,21)内側の上部との間に間隙(G)が配され
ることを特徴とする請求項1から6のいずれか記載の液
体中気泡除去装置。
7. A gap (G) is provided between an upper portion of the filter (14, 24) and an upper portion inside the container body (11, 21). The apparatus for removing bubbles in liquid according to the above.
【請求項8】 容器本体(11,21)の上部に内方に
傾斜形状のテーパ部(11a,21a)が配されること
を特徴とする請求項1から7のいずれか記載の液体中気
泡除去装置。
8. An air bubble in a liquid according to claim 1, wherein an inwardly tapered portion (11a, 21a) is disposed in an upper portion of the container body (11, 21). Removal device.
JP8210311A 1996-08-08 1996-08-08 Device for removing bubble in liquid Pending JPH1043293A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8210311A JPH1043293A (en) 1996-08-08 1996-08-08 Device for removing bubble in liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8210311A JPH1043293A (en) 1996-08-08 1996-08-08 Device for removing bubble in liquid

Publications (1)

Publication Number Publication Date
JPH1043293A true JPH1043293A (en) 1998-02-17

Family

ID=16587317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8210311A Pending JPH1043293A (en) 1996-08-08 1996-08-08 Device for removing bubble in liquid

Country Status (1)

Country Link
JP (1) JPH1043293A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000020108A1 (en) * 1998-10-02 2000-04-13 Karasawa Fine Co., Ltd. Method of producing fine particle dispersions
JP2004508183A (en) * 2000-09-13 2004-03-18 マイクロリス・コーポレイシヨン Liquid filtration device
US7850636B2 (en) 2005-10-03 2010-12-14 Jms Co., Ltd. Closed-type blood reservoir and extracorporeal blood circulation apparatus using the same
JP2011505976A (en) * 2007-12-13 2011-03-03 ボシュ・アンド・ロム・インコーポレイテッド Air separator for eye surgery system
JP2011092498A (en) * 2009-10-30 2011-05-12 Junken Medical株式会社 Chamber for extracorporeal circulation circuit
JP2014079726A (en) * 2012-10-18 2014-05-08 Arai Tekkosho:Kk Method and device of deaerating foam-containing liquid
CN108654147A (en) * 2018-08-28 2018-10-16 湖南大三湘茶油股份有限公司 Edible oil froth breaker
JP2019202256A (en) * 2018-05-22 2019-11-28 株式会社ディスコ Gas-liquid separation mechanism
JP2020002935A (en) * 2018-07-02 2020-01-09 株式会社デンソー Reserve tank

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000020108A1 (en) * 1998-10-02 2000-04-13 Karasawa Fine Co., Ltd. Method of producing fine particle dispersions
JP2004508183A (en) * 2000-09-13 2004-03-18 マイクロリス・コーポレイシヨン Liquid filtration device
US7850636B2 (en) 2005-10-03 2010-12-14 Jms Co., Ltd. Closed-type blood reservoir and extracorporeal blood circulation apparatus using the same
JP2011505976A (en) * 2007-12-13 2011-03-03 ボシュ・アンド・ロム・インコーポレイテッド Air separator for eye surgery system
JP2011092498A (en) * 2009-10-30 2011-05-12 Junken Medical株式会社 Chamber for extracorporeal circulation circuit
JP2014079726A (en) * 2012-10-18 2014-05-08 Arai Tekkosho:Kk Method and device of deaerating foam-containing liquid
JP2019202256A (en) * 2018-05-22 2019-11-28 株式会社ディスコ Gas-liquid separation mechanism
JP2020002935A (en) * 2018-07-02 2020-01-09 株式会社デンソー Reserve tank
WO2020009030A1 (en) * 2018-07-02 2020-01-09 株式会社デンソー Reserve tank
CN108654147A (en) * 2018-08-28 2018-10-16 湖南大三湘茶油股份有限公司 Edible oil froth breaker

Similar Documents

Publication Publication Date Title
JPS648562B2 (en)
US4676771A (en) Arterial blood filter
US5298016A (en) Apparatus for separating plasma and other wastes from blood
JP3575620B2 (en) Method and apparatus for continuous adjustment of cell suspension
US4482342A (en) Blood processing system for cell washing
JP3577444B2 (en) Blood processing centrifuge bowl and method for collecting plasma fraction from whole blood
US5405308A (en) Disposable centrifuge rotor and core for blood processing
US8226537B2 (en) Blood processing apparatus with cell separation chamber with baffles
CA1261765A (en) Method and apparatus for separation of matter from suspension
EP0194271B1 (en) Closed hemapheresis system
JPH01148266A (en) Blood filter
US20090065424A1 (en) Circular centrifugation chamber for separation of blood
JP2002538956A (en) Centrifuge and method for separating fluid components
JPH07284529A (en) Centrifuge bowl to process blood and its method
JPH09276396A (en) Centrifugal separator bowl for hematocrit
WO1990007383A1 (en) Disposable centrifuge bowl for blood processing
JPH09508564A (en) Blood filter having concentric folds and method of using the same
CN1073614A (en) Method and apparatus from the biological fluid separated plasma
JPH1043293A (en) Device for removing bubble in liquid
US4434061A (en) Solids-liquid separation
JP2001061955A (en) Autotransfusion device and method
JPH0126707B2 (en)
US6276936B1 (en) Dental separator for solids from a solids/liquid mixture
JPS63102764A (en) Blood storage tank
JPH01148265A (en) Blood filter

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20051220

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060104

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20060509