JPH0334244Y2 - - Google Patents

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Publication number
JPH0334244Y2
JPH0334244Y2 JP1985144459U JP14445985U JPH0334244Y2 JP H0334244 Y2 JPH0334244 Y2 JP H0334244Y2 JP 1985144459 U JP1985144459 U JP 1985144459U JP 14445985 U JP14445985 U JP 14445985U JP H0334244 Y2 JPH0334244 Y2 JP H0334244Y2
Authority
JP
Japan
Prior art keywords
liquid
cylindrical body
inlet
inflow
casing
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
Application number
JP1985144459U
Other languages
Japanese (ja)
Other versions
JPS6256105U (en
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 filed Critical
Priority to JP1985144459U priority Critical patent/JPH0334244Y2/ja
Priority to DE19863620999 priority patent/DE3620999A1/en
Priority to GB8617481A priority patent/GB2180474B/en
Priority to KR1019860007875A priority patent/KR910001892B1/en
Publication of JPS6256105U publication Critical patent/JPS6256105U/ja
Application granted granted Critical
Publication of JPH0334244Y2 publication Critical patent/JPH0334244Y2/ja
Expired legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/24Multiple arrangement thereof
    • B04C5/28Multiple arrangement thereof for parallel flow
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D19/00Degasification of liquids
    • B01D19/0042Degasification of liquids modifying the liquid flow
    • B01D19/0052Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
    • B01D19/0057Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused the centrifugal movement being caused by a vortex, e.g. using a cyclone, or by a tangential inlet

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Cyclones (AREA)

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は塗料、コーテイング液、ワニス、ニナ
メル、インキ、接着剤、ミルク、糖密等の食用
液、スラリー、薬液、液状化成品、冷却水、洗浄
液、漂白液、洗剤、各種廃液、下水、冷暖房設備
用流体あるいはスポンジ、エマルジヨン、ラテツ
クス、更には潤滑油、油圧作動油等の鉱油、等に
混入する気泡を分離させて除去させるために用い
るもので、特に、大流量の液体中の気泡除去に有
効な気泡除去装置に関するものである。
[Detailed description of the invention] [Field of industrial application] This invention is applicable to paints, coating liquids, varnishes, nyamels, inks, adhesives, milk, edible liquids such as molasses, slurries, chemical liquids, liquid chemical products, and cooling water. Used to separate and remove air bubbles mixed in cleaning liquids, bleaching liquids, detergents, various waste liquids, sewage, fluids for air conditioning equipment, sponges, emulsions, latex, mineral oils such as lubricating oils and hydraulic oils, etc. In particular, the present invention relates to a bubble removal device that is effective in removing bubbles from a liquid with a large flow rate.

[従来の技術] 上述の如き各種液体中に気泡が含まれている場
合、この気泡が機器の損傷、エアーレーシヨン及
びキヤビテーシヨンによるエロージヨン、騒音、
製品不良、例えば気泡による塗工面上の未塗工等
を引き起こす原因となるため、気泡を液体中より
分離除去することが必要である。
[Prior Art] When air bubbles are included in the various liquids mentioned above, these air bubbles can cause damage to equipment, erosion due to air ration and cavitation, noise,
It is necessary to separate and remove air bubbles from the liquid because they can cause product defects, such as non-coating on the coated surface due to air bubbles.

従来の気泡除去装置としては、第3図に示す如
く、両端を蓋bとcで閉塞した円筒体aの一端部
に、ポンプdより吐出された液体を円筒体a内に
流入させるための流入口eを接線方向に設けると
共に、円筒体aの他端の蓋b中心部に液体の流出
口fを設け、更に、上記円筒体aの一端の蓋c中
心部に気体抜口gを設け、上記流出口fは流出側
配管hを介して液体タンクi等に接続させ、気体
抜口gには開閉弁k付きの放気管jを接続した構
成としてある。
As shown in FIG. 3, a conventional bubble removing device has a cylindrical body a whose both ends are closed with lids b and c, and a flow for causing liquid discharged from a pump d to flow into the cylindrical body a. An inlet e is provided in the tangential direction, a liquid outlet f is provided at the center of the lid b at the other end of the cylindrical body a, and a gas outlet g is provided at the center of the lid c at one end of the cylindrical body a, The outlet f is connected to a liquid tank i or the like via an outlet pipe h, and the gas outlet g is connected to an air discharge pipe j with an on-off valve k.

上記の気泡除去装置では、気泡の混入した液体
がポンプdによつて円筒体a内に供給される場
合、接線方向に開口する流入口eから液体が所定
の流速で流入するめ、円筒体aの内面に沿つた旋
回流となる。この旋回流は、遠心力によつて流入
口e付近の円筒体a内で最も大きく、下流側に移
行するに従い小さくなつて軸流となり、液体は流
出口fから流出され、上記遠心力により円筒体の
軸心部に多くの気泡が集合する。これは、円筒体
aの軸心部に生ずる圧力が、流入口e付近が最も
低く下流に向つて徐々に高くなり最高値を示した
後低くなるという圧力分布となるからであり、こ
の圧力分布により、気泡は流入口e付近の軸心部
に集合して円筒体a軸心部に気体柱lを形成する
ことになる。この集合した気泡は気体抜口gから
外部へ排出される。
In the above bubble removing device, when liquid containing air bubbles is supplied into the cylinder a by the pump d, the liquid flows at a predetermined flow rate from the inlet e opening in the tangential direction. A swirling flow follows the inner surface. This swirling flow is largest in the cylinder a near the inlet e due to the centrifugal force, and becomes smaller as it moves downstream to become an axial flow. The liquid flows out from the outlet f, and the centrifugal force Many air bubbles gather around the axis of the body. This is because the pressure generated at the axial center of the cylinder a has a pressure distribution where it is lowest near the inlet e, gradually increases downstream, reaches a maximum value, and then decreases, and this pressure distribution As a result, the bubbles gather at the axial center near the inlet e and form a gas column l at the axial center of the cylinder a. The collected bubbles are discharged to the outside from the gas outlet g.

第3図に示す気泡除去装置は、その性能を発揮
するためには小径の円筒である事が必要でその結
果小流量を対応とせざるを得ない。
The bubble removing device shown in FIG. 3 needs to be a cylinder with a small diameter in order to exhibit its performance, and as a result, it is forced to handle a small flow rate.

[考案が解決しようとする問題点] ところが、近年、大流量の液体を扱う配管途中
で気泡を除去する必要性が生じているが、このよ
うな第3図の形式で大流量の液体に含まれる気泡
を除去するようにするには、液体の流入速度、流
入圧力を大にせざるを得ない。これは、液体供給
用のポンプdの吐出圧は本来極小であるべきで、
気泡ガスの液体中への溶解、気泡圧縮、キヤビテ
ーシヨン及びそれに起因するエロージヨンを回避
しつつ液体を気泡除去装置に移送する意図に相反
するものである。
[Problem that the invention aims to solve] However, in recent years, there has been a need to remove air bubbles from the middle of piping that handles large flow rates of liquids, and this method, as shown in Figure 3, is used to remove air bubbles from pipes that handle large flow rates of liquids. In order to remove the air bubbles, it is necessary to increase the inflow velocity and inflow pressure of the liquid. This is because the discharge pressure of pump d for liquid supply should originally be extremely small.
This is contrary to the intention of transferring the liquid to the bubble removal device while avoiding dissolution of bubble gas into the liquid, bubble compression, cavitation and resulting erosion.

又、第3図に示す従来の気泡除去装置では、円
筒体aの内部の掃除を行うことができないため、
例えばコーテイング液のように粘性物質を含む液
体を扱う場合、円筒体aや気体抜口gが閉塞する
等のトラブルの発生を防止できないという不具合
があつた。
Furthermore, since the conventional bubble removing device shown in FIG. 3 cannot clean the inside of the cylinder a,
For example, when handling a liquid containing a viscous substance such as a coating liquid, there is a problem in that it is impossible to prevent troubles such as clogging of the cylinder a or the gas outlet g.

そこで、本考案は、大流量液体中の気泡を流入
圧力を上昇させる必要なく効率よく除去でき、且
つ掃除を容易に行い得るようにしようとするもの
である。
Therefore, the present invention aims to make it possible to efficiently remove bubbles from a large flow rate liquid without increasing the inflow pressure, and to facilitate cleaning.

[問題点を解決するための手段] 本考案は、複数本の気泡集合用の円筒体を同一
方向に並置しその各一端の接線方向より液体を流
入させるための流入口を設け、各円筒体の上記流
入口側端部の外周に、液体が供給される流入側ケ
ーシングと、該流入側ケーシングに着脱自在に取
り付けられ且つ各円筒体の流入口側端部を閉塞す
る下部閉塞板とによつて形成される1つの流入側
空間部を設けると共に、各円筒体の流出側を、流
出側ケーシングと、該流出側ケーシングに着脱自
在に取り付けられ且つ下流側配置が接続される閉
塞板とによつて形成される1つの流出側空間部に
開口させ、上記各円筒体の流入側の閉塞部に気体
を放出させる通路を設け、又、液体の流出側空間
部の下流側に、液体通過時に流量に対し0.05Kg
f/cm2以上の背圧を与える抵抗体を設けた構成と
する。
[Means for Solving the Problems] The present invention consists of arranging a plurality of cylinders for collecting bubbles in the same direction, providing an inlet for liquid to flow in from the tangential direction at one end of each cylinder, and An inflow side casing to which liquid is supplied is provided around the outer periphery of the inflow side end of the cylindrical body, and a lower closing plate that is detachably attached to the inflow side casing and closes the inflow side end of each cylindrical body. In addition, the outflow side of each cylindrical body is formed by an outflow side casing and a closing plate detachably attached to the outflow side casing and connected to the downstream arrangement. A passageway is provided which opens into one outflow space formed by the cylinders and releases gas from the closed part on the inflow side of each of the cylindrical bodies. 0.05Kg for
The structure includes a resistor that provides a back pressure of f/cm 2 or more.

[作用] 複数本の円筒体の各一端に接線方向に開口させ
た流入口から液体を流入させると、加速度による
遠心力で微細気泡が各円筒体ごとに軸心部に集合
させられ、上記各円筒体の液体出口側に背圧を与
えることによつて上記集合された気泡が気体排出
口から円筒体外へ排出される。
[Operation] When liquid is allowed to flow in from the inlet opening tangentially at one end of each of the plurality of cylindrical bodies, microbubbles are gathered at the axial center of each cylindrical body due to the centrifugal force caused by the acceleration, and each of the above-mentioned By applying back pressure to the liquid outlet side of the cylindrical body, the collected bubbles are discharged from the cylindrical body through the gas outlet.

又、流入側ケーシングから下部閉塞板を取り外
せば、流入側空間部及び各円筒体の内部を容易に
掃除でき、流出側ケーシングから閉塞板を取り外
せば、流出側空間部の内部の掃除も容易に行え
る。
Furthermore, by removing the lower blocking plate from the inflow side casing, the inflow side space and the inside of each cylindrical body can be easily cleaned, and by removing the blocking plate from the outflow side casing, the inside of the outflow side space can be easily cleaned. I can do it.

[実施例] 以下、図面に基づき本考案の実施例を説明す
る。
[Example] Hereinafter, an example of the present invention will be described based on the drawings.

第1図及び第2図は本考案の一実施例を示すも
ので、複数本(図面では4本)の気泡集合用の円
筒体2を同一方向に並置し、該各円筒体2の一端
(下端)に、接線方向より液体を流入させるため
の流入口8を1個又は複数個(図示の例は2個)
設け、上記各円筒体2の流入口8側端部の外周
に、後述する流入側配管7から液体が供給される
流入側ケーシング20と、該流入側ケーシング2
0に着脱自在に取り付けられ且つ各円筒体2の流
入口8側端部を閉塞する下部閉塞板4とによつて
形成される1つの流入側空間部5を設け、上記流
入側ケーシング20の側部に、液体供給用ポンプ
6にて圧送される液体を流入させるための流入側
配管7を接続し、又、上記各円筒体2の他端(上
端)を、流出側ケーシング3と、該流出側ケーシ
ング3に着脱自在に取り付けられ且つ下流側配管
17が接鮮される閉塞板15とによつて形成され
る1つの流出側空間部9に開口させ、上記流入側
配管7を通して流入側空間部5内に流入した液体
が各円筒体2内に流入口8から供給されて旋回流
を形成し各円筒体2の上端開口より流出側空間部
9に流出するようにする。
FIGS. 1 and 2 show an embodiment of the present invention, in which a plurality (four in the drawing) of cylinders 2 for collecting bubbles are arranged side by side in the same direction, and one end of each cylinder 2 ( (lower end), one or more inlets 8 (two in the illustrated example) for allowing liquid to flow in from the tangential direction.
An inflow side casing 20 is provided on the outer periphery of the end on the inflow port 8 side of each of the cylindrical bodies 2, and the inflow side casing 20 is supplied with liquid from an inflow side piping 7, which will be described later.
One inflow side space 5 formed by a lower closing plate 4 which is detachably attached to the inlet casing 20 and which closes the inlet 8 side end of each cylindrical body 2 is provided. An inflow side pipe 7 for inflowing the liquid pumped by the liquid supply pump 6 is connected to the part, and the other end (upper end) of each cylindrical body 2 is connected to the outflow side casing 3 and the outflow side pipe 7. It opens into one outflow side space 9 formed by a closing plate 15 that is detachably attached to the side casing 3 and on which the downstream piping 17 is freshened, and passes through the inflow side piping 7 to the inflow side space. The liquid that has flowed into each cylindrical body 5 is supplied from the inlet 8 into each cylindrical body 2 to form a swirling flow and flow out from the upper end opening of each cylindrical body 2 to the outflow side space 9.

上記下部閉塞板4の下面側には、放気側ケーシ
ング21を着脱自在に取り付けることにより放気
側空間部10を形成して、該放気側空間部10と
上記各円筒体2の軸心部とを、下部閉塞板4に
各々設けた気体抜口11にて連通させ、各円筒体
2に生ずる旋回流により軸心部に集合された気泡
が各気体抜口11から放気側空間部10へ排出さ
れるようにする。上記放気側空間部10の下部に
は、気体放出口12を設け、該気体放出口12
に、途中に気体放出弁14を有する気体放出管1
3を接続させる。又、上記流出側ケーシング3に
取り付けられる閉塞板15にオリフイス16を組
込んだり、上記閉塞板15に接続される下流側配
管17の断面積を小としたり、該配管17に流出
側絞り弁18を設け、これを絞るなどして各円筒
体2内で分離された気泡が気体抜口11を通り放
気側空間部10へ排出する分流が発生するよう背
圧を0.05Kgf/cm2以上え得るようにしてある。
An air release side casing 21 is removably attached to the lower surface side of the lower blocking plate 4 to form an air release side space 10, and the axis of the air release side space 10 and each of the cylindrical bodies 2 is The air bubbles collected at the axial center by the swirling flow generated in each cylindrical body 2 are communicated with each other through gas vents 11 provided in the lower closing plate 4, and the air bubbles are transferred from each gas vent 11 to the air discharge side space. 10. A gas release port 12 is provided in the lower part of the air release side space 10, and the gas release port 12 is provided with a gas release port 12.
, a gas release pipe 1 having a gas release valve 14 in the middle
Connect 3. Furthermore, an orifice 16 may be incorporated into the blocking plate 15 attached to the outlet casing 3, the cross-sectional area of the downstream pipe 17 connected to the blocking plate 15 may be reduced, or an outlet throttle valve 18 may be installed in the pipe 17. A back pressure of 0.05 Kgf/cm 2 or more is set so that the air bubbles separated in each cylindrical body 2 pass through the gas vent 11 and are discharged to the air discharge side space 10 by squeezing the air bubbles. I am trying to get it.

なお、液体は円筒体2内を旋回流から軸流に移
りつつ下流側に移行するが、これに伴ない上記各
円筒体2の軸心部に生ずる圧力分布は、流入口8
付近が最も低く下流(図上上方)に向つて徐々に
高くなり最高値を示した後低くなるという分布と
なりこの圧力分布により気泡は流入口8付近の軸
中心部に集合して円筒体の軸心部に気体柱を形成
するようにしてある。19は圧力計である。
Note that the liquid moves from a swirling flow to an axial flow inside the cylinder 2 and moves downstream, but the pressure distribution that occurs at the axial center of each cylinder 2 due to this changes at the inlet 8.
The pressure distribution is lowest near the area, and gradually increases toward the downstream (upper part of the figure), reaches the highest value, and then decreases. Due to this pressure distribution, the air bubbles gather at the center of the axis near the inlet 8, and the air bubbles move toward the axis of the cylinder. A gas column is formed in the core. 19 is a pressure gauge.

今、ポンプ6から吐出された大量の液体が流入
側配管7から流入側空間部5内に流入すると、こ
こから上記液体が各円筒体2の流入口8から円筒
体2内に流入する。各円筒体2内に流入した液体
は、旋回による遠心力によつて軸心部に気泡を集
合させる。この場合、円筒体2の軸中心部の圧力
分布は、前記した如く、流入口8付近が最も低
く、下流に向つて徐々に高くなり最高値を示した
後、低くなるようになつているため、気泡は旋回
中心軸付近で且つ流入口8付近から最高圧力位置
までの間に集結合する。円筒体2で気泡を分離し
た液体は円筒体2の下流側(上端側)よりオリフ
イス16、小径配管17、流出側絞り弁18など
による抵抗体を経て流出する。
Now, when a large amount of liquid discharged from the pump 6 flows into the inflow side space 5 from the inflow side piping 7, the liquid flows from there into the cylindrical body 2 through the inlet port 8 of each cylindrical body 2. The liquid flowing into each cylindrical body 2 collects bubbles at the axial center due to the centrifugal force caused by the swirling. In this case, the pressure distribution at the axial center of the cylindrical body 2 is lowest near the inlet 8, as described above, gradually increases toward the downstream, reaches a maximum value, and then decreases. , the bubbles are concentrated near the center axis of rotation and between the vicinity of the inlet 8 and the highest pressure position. The liquid from which bubbles have been separated in the cylindrical body 2 flows out from the downstream side (upper end side) of the cylindrical body 2 through a resistor such as an orifice 16, a small-diameter pipe 17, and an outflow-side throttle valve 18.

円筒体2の軸心部の流入口8側は、前記の如く
旋回による大きな遠心力のため、円筒体2の流出
側以降に流体負荷が存在しない場合、負圧にな
り、下部閉塞板4に気体抜口11を設けて集合気
泡を放出させようとしても放出できない。これ
は、円筒体2の流入口8付近の軸中心部の圧力
が、液体の流入速度、円筒体の内径等の条件によ
り異なるけれども、液体流出側以降の背圧が零で
あれば集合気泡を排出できないからである。この
ため、円筒体2の流出側開口以降に、オリフイス
16、絞り弁18、断面積の小なる配管17等の
抵抗体を接続し、背圧を0.05Kgf/cm2以上与え、
気泡を気体抜口11から放気側空間部10に排出
させるようにする。上記背圧は、いかなる流体粘
度、気泡径、円筒体寸法等の諸条件に対しても
0.05Kgf/cm2以上であるべきことが経験より得ら
れた。上記背圧をチエツクする手段としては、流
入側の圧力計19がある。
Due to the large centrifugal force caused by the rotation as described above, the inlet 8 side of the axial center of the cylindrical body 2 becomes negative pressure when there is no fluid load after the outflow side of the cylindrical body 2, and the lower blockage plate 4 Even if an attempt is made to release the aggregated air bubbles by providing a gas vent 11, the air bubbles cannot be released. Although the pressure at the center of the axis near the inlet 8 of the cylinder 2 varies depending on conditions such as the liquid inflow speed and the inner diameter of the cylinder, if the back pressure after the liquid outflow side is zero, the air bubbles will collect. This is because it cannot be discharged. For this reason, a resistor such as an orifice 16, a throttle valve 18, and a pipe 17 with a small cross-sectional area is connected after the outlet opening of the cylindrical body 2, and a back pressure of 0.05 Kgf/cm 2 or more is applied.
Air bubbles are discharged from the gas outlet 11 to the air discharge side space 10. The above back pressure is independent of various conditions such as fluid viscosity, bubble diameter, cylinder size, etc.
Experience has shown that it should be 0.05 Kgf/cm 2 or more. As means for checking the back pressure, there is a pressure gauge 19 on the inflow side.

放気側空間部10に排出された気泡は、気体放
出口12から放出管13を経て放出されることに
なる。
The bubbles discharged into the air discharge side space 10 are discharged from the gas discharge port 12 via the discharge pipe 13.

又、各円筒体2の外周部のほとんどを露出させ
てあるため、各円筒体2外周部の液による汚れを
減少させることができると共に、閉塞板15、放
気側ケーシング21、及び下部閉塞板4を取り外
せるようにしてあるため、流出側空間部9、放気
側空間部10、流入側空間部5及び各円筒体2の
内部の掃除を容易に行うことができ、メンテナン
ス上きわめて有利となる。
Furthermore, since most of the outer circumferential portion of each cylindrical body 2 is exposed, it is possible to reduce contamination of the outer circumferential portion of each cylindrical body 2 with liquid, and also to prevent the closing plate 15, the air discharge side casing 21, and the lower closing plate 4 can be removed, the outflow side space 9, the air discharge side space 10, the inflow side space 5, and the inside of each cylindrical body 2 can be easily cleaned, which is extremely advantageous in terms of maintenance. .

尚、上記各実施例では、各円筒体2を同径の直
管としたものを示したが、下流側の径が大きくな
るテーパー付きとしてもよい。また、多数本の円
筒体の下流側に個々に抵抗を組入れてもよい。更
に又個々の円筒体は必らずしも同径のものでなく
てもよい。
In each of the above embodiments, each cylindrical body 2 is shown as a straight tube with the same diameter, but it may be tapered so that the diameter on the downstream side becomes larger. Further, resistors may be individually incorporated on the downstream side of a large number of cylindrical bodies. Furthermore, the individual cylindrical bodies do not necessarily have to have the same diameter.

[考案の効果] 以上述べた如く本考案の気泡除去装置によれ
ば、複数本の気泡集合用の円筒体の各一端に接線
方向より液体を流入させるために流入口を設け
て、各円筒体の上記流入口側端部を囲む1つの流
入側空間部を設け、該流入側空間部に流入側配管
を接続し、又、各円筒体の流出側を1つの流出側
空間部に開口させ、流入側空間部に入つた液体が
各円筒体内に流入口から流入して旋回流となり、
このときの遠心力によつて気泡を旋回流軸心部に
集結合させるようにし、液体の流出側に0.05Kg
f/cm2以上の背圧を与えるようにし、集結合した
気泡を流入側軸中心より抜いて外部へ放出させる
ようにしてあるので、大流量の液体であつても小
流量のものと差異なく液体中の気泡を効率よく除
去でき、しかも流入圧力を上昇させることなく気
泡を除去でき、集結合した気泡は確実に外部へ放
出でき、気泡のない品質のよい製品が得られる、
等の優れた効果を奏し得る。
[Effects of the invention] As described above, according to the bubble removing device of the present invention, an inlet is provided at each end of each cylinder for collecting bubbles to allow liquid to flow in from a tangential direction. providing one inflow side space surrounding the inflow side end of the cylindrical body, connecting an inflow side piping to the inflow side space, and opening the outflow side of each cylindrical body into one outflow side space; The liquid that entered the inlet side space flows into each cylinder from the inlet and becomes a swirling flow.
At this time, the centrifugal force causes the bubbles to concentrate at the axis of the swirling flow, and 0.05Kg is applied to the liquid outlet side.
By applying a back pressure of f/cm 2 or more, the collected bubbles are pulled out from the center of the inlet shaft and released to the outside, so even a large flow of liquid is no different from a small flow of liquid. It is possible to efficiently remove air bubbles from the liquid without increasing the inflow pressure, and the collected air bubbles can be reliably released to the outside, resulting in a high-quality product without air bubbles.
It can produce excellent effects such as

更に、本考案の気泡除去装置によれば、流入側
ケーシングに対して下部閉塞板を、又、流出側ケ
ーシングに対して閉塞板を夫々着脱自在に取り付
けてあるため、流入側空間部や流出側空間部、並
びに各円筒体の内部の掃除を容易に行うことがで
き、メンテナンス上きわめて有利となり、液体中
に含まれる粘性物質の付着等によるトラブルの発
生を未然に防止できる。
Furthermore, according to the bubble removal device of the present invention, the lower closing plate is detachably attached to the inlet side casing and the outlet side casing is detachably attached, so that the inlet side space and the outlet side space are separated. The space and the inside of each cylindrical body can be easily cleaned, which is extremely advantageous in terms of maintenance, and troubles caused by adhesion of viscous substances contained in the liquid can be prevented.

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

第1図は本考案の装置の一実施例を示す断面
図、第2図は第1図の方向よりの断面図、第3
図は従来の装置の概要図である。 2は円筒体、5は流入側空間部、8は流入口、
9は流出側空間部、10は放気側空間部、11は
気体抜口、16はオリフイス、18は流出側絞り
弁を示す。
Fig. 1 is a sectional view showing one embodiment of the device of the present invention, Fig. 2 is a sectional view taken from the direction of Fig. 1, and Fig. 3 is a sectional view showing an embodiment of the device of the present invention.
The figure is a schematic diagram of a conventional device. 2 is a cylindrical body, 5 is an inflow side space, 8 is an inflow port,
9 is an outflow side space, 10 is an air discharge side space, 11 is a gas outlet, 16 is an orifice, and 18 is an outflow side throttle valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 複数本の気泡集合用の円筒体を同一方向に並置
してその各一端に接線方向より液体を流入させる
ための流入口を設け、各円筒体の上記流入口側端
部の外周に、液体が供給される流入側ケーシング
と、該流入側ケーシングに着脱自在に取り付けら
れ且つ各円筒体の流入口側端部を閉塞する下部閉
塞板とによつて形成される1つの流入側空間部を
設けると共に、各円筒体の流出側を、流出側ケー
シングと、該流出側ケーシングに着脱自在に取り
付けられ且つ下流側配管が接続される閉塞板とに
よつて形成される1つの流出側空間部に開口さ
せ、上記各円筒体の流入側の閉塞部に気体を放出
させる通路を設け、又、液体の流出側空間部の下
流側に、液体通過時に流量に対し0.05Kgf/cm2
上の背圧を与える抵抗体を設けたことを特徴とす
る気泡除去装置。
A plurality of cylindrical bodies for collecting bubbles are arranged side by side in the same direction, and an inlet is provided at one end of each cylinder to allow liquid to flow in from a tangential direction. One inflow side space formed by the supplied inflow side casing and a lower closing plate that is detachably attached to the inflow side casing and closes the inlet side end of each cylindrical body, and , the outflow side of each cylindrical body is opened to one outflow side space formed by an outflow side casing and a closing plate that is detachably attached to the outflow side casing and to which the downstream piping is connected. , provide a passage for releasing gas in the closed part on the inlet side of each of the cylinders, and apply a back pressure of 0.05 Kgf/cm 2 or more to the flow rate on the downstream side of the liquid outlet space when the liquid passes through. A bubble removing device characterized by being provided with a resistor.
JP1985144459U 1985-09-21 1985-09-21 Expired JPH0334244Y2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP1985144459U JPH0334244Y2 (en) 1985-09-21 1985-09-21
DE19863620999 DE3620999A1 (en) 1985-09-21 1986-06-23 DEVICE FOR REMOVING BUBBLES
GB8617481A GB2180474B (en) 1985-09-21 1986-07-17 Device for removing bubbles
KR1019860007875A KR910001892B1 (en) 1985-09-21 1986-09-20 Bubble removing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1985144459U JPH0334244Y2 (en) 1985-09-21 1985-09-21

Publications (2)

Publication Number Publication Date
JPS6256105U JPS6256105U (en) 1987-04-07
JPH0334244Y2 true JPH0334244Y2 (en) 1991-07-19

Family

ID=15362749

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1985144459U Expired JPH0334244Y2 (en) 1985-09-21 1985-09-21

Country Status (4)

Country Link
JP (1) JPH0334244Y2 (en)
KR (1) KR910001892B1 (en)
DE (1) DE3620999A1 (en)
GB (1) GB2180474B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5514206A (en) * 1994-04-15 1996-05-07 Consolidated Papers, Inc. Air/gas separator device
CN102878813B (en) * 2012-10-26 2014-09-24 烽火通信科技股份有限公司 Cooling device used in hot environment
CN110052060B (en) * 2019-04-24 2022-07-01 杭州科百特过滤器材有限公司 Hollow fiber degassing membrane module

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE501733A (en) * 1950-03-09
JPS59190307U (en) * 1983-06-01 1984-12-17 石川島播磨重工業株式会社 Air bubble remover

Also Published As

Publication number Publication date
JPS6256105U (en) 1987-04-07
KR870002858A (en) 1987-04-13
KR910001892B1 (en) 1991-03-30
DE3620999A1 (en) 1987-04-02
GB8617481D0 (en) 1986-08-28
GB2180474B (en) 1989-09-13
GB2180474A (en) 1987-04-01

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