JPH044002A - Defoaming device - Google Patents
Defoaming deviceInfo
- Publication number
- JPH044002A JPH044002A JP10044590A JP10044590A JPH044002A JP H044002 A JPH044002 A JP H044002A JP 10044590 A JP10044590 A JP 10044590A JP 10044590 A JP10044590 A JP 10044590A JP H044002 A JPH044002 A JP H044002A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- liq
- gas
- tube
- bubbles
- 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
- 238000000926 separation method Methods 0.000 claims abstract description 25
- 239000012528 membrane Substances 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000005486 microgravity Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 230000006837 decompression Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- -1 polytetrafluoroethylene Polymers 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、微小重力環境等で用いられる脱泡装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a defoaming device used in microgravity environments and the like.
〔従来の技術]
従来の多孔質の気液分離膜を用いた脱泡装置においては
、分離膜製のチューブ内又は分離膜の表面を泡を含む液
体を流し、分離膜に付着した泡を分離膜両側の圧力差に
より取り除くようにしている。[Prior art] In a conventional defoaming device using a porous gas-liquid separation membrane, a liquid containing bubbles is passed through a tube made of the separation membrane or on the surface of the separation membrane, and the bubbles adhering to the separation membrane are separated. It is removed by the pressure difference on both sides of the membrane.
第3図に、その1例として、従来の平膜式の脱泡装置を
示す。入口02及び出口03をもつ水通路O1の底部に
、多孔質の気液分離膜04を水道路01の全長にわたっ
て設け、同分離膜04の下方に減圧室05を設け、分離
膜05両側の圧力差によって、水通路O1を通る水から
気泡を分離するようにしている。FIG. 3 shows a conventional flat membrane defoaming device as an example. A porous gas-liquid separation membrane 04 is provided at the bottom of the water passage O1 having an inlet 02 and an outlet 03 over the entire length of the water passage 01, and a decompression chamber 05 is provided below the separation membrane 04, so that the pressure on both sides of the separation membrane 05 is The difference separates air bubbles from the water passing through the water passage O1.
(発明が解決しようとする課題〕
従来の多孔質の気液分離膜を使用した脱泡装置では、液
中の泡を多孔質膜に効率よく付着させるため、液通路幅
はある程度狭く、流路長は長くとる必要がある。このた
め、処理能力を高めるには、液通路を長く、数多く必要
となり装置としては大型になる。(Problems to be Solved by the Invention) In a conventional defoaming device using a porous gas-liquid separation membrane, in order to make bubbles in the liquid adhere to the porous membrane efficiently, the width of the liquid passage is narrow to some extent, Therefore, in order to increase the processing capacity, a large number of long liquid passages are required, resulting in a large device.
本発明は、以上の従来の多孔質の気液分離膜を使用した
脱泡装置の欠点を解決しようとするものである。The present invention aims to solve the above-mentioned drawbacks of conventional defoaming devices using porous gas-liquid separation membranes.
〔課題を解決するための手段]
本発明の脱泡装置は、泡を含む液が流れる容器、同容器
内に液の流れを横切って配置された複数の多孔質の気液
分離膜製のチューブ、及び同チューブ内を減圧する排気
装置を備えている。[Means for Solving the Problems] The defoaming device of the present invention includes a container through which a liquid containing bubbles flows, and a plurality of tubes made of a porous gas-liquid separation membrane arranged in the container across the flow of the liquid. , and an exhaust device to reduce the pressure inside the tube.
この泡を含む液体は、液体の流れを横切って配置され内
側を減圧した複数の多孔質の気液分離膜製チューブのま
わりを流れることによって、液中の泡と多孔質の気液分
離膜との接触する頻度が高くなり、脱泡効率が向上する
。The bubble-containing liquid flows around multiple porous gas-liquid separation membrane tubes that are placed across the flow of the liquid and have reduced pressure inside, thereby separating the bubbles in the liquid and the porous gas-liquid separation membrane. This increases the frequency of contact between the two and improves the defoaming efficiency.
これにより、多量の液を小型の装置で処理できることと
なる。This allows a large amount of liquid to be processed with a small device.
C実施例〕
本発明の一実施例を、第1図及び第2図によって説明す
る。C Embodiment] An embodiment of the present invention will be described with reference to FIGS. 1 and 2.
本実施例は、脱泡部10と真空ポンプ等の真空排気装置
11から成る。This embodiment consists of a defoaming section 10 and a vacuum evacuation device 11 such as a vacuum pump.
脱泡部10は、第2図に示すように、泡を含む液の液入
口4と液出口5を両側にもち液が液入口4から液出口5
へ向ってその内部を流れる断面矩形の容器1、及び容器
1内の液の流れに直角に水平方向に網目状に配置された
多数のチューブ2から成っている。各チューブ2は、多
孔質の疏水性の気液分離膜、例えば、孔径0.02〜1
5μ面の多孔質のポリ四弗化エチレン等の弗素樹脂製の
膜で構成されており、同チューブ2の内側は、真空排気
装置11 (最大真空圧I Xl0−’torr)に接
続されている。As shown in FIG. 2, the defoaming unit 10 has a liquid inlet 4 and a liquid outlet 5 on both sides of the liquid containing bubbles, and the liquid flows from the liquid inlet 4 to the liquid outlet 5.
It consists of a container 1 with a rectangular cross section through which the liquid flows, and a number of tubes 2 arranged horizontally in a mesh pattern at right angles to the flow of liquid in the container 1. Each tube 2 is made of a porous hydrophobic gas-liquid separation membrane, for example, with a pore size of 0.02 to 1.
It is composed of a membrane made of a fluororesin such as polytetrafluoroethylene with a porous surface of 5μ, and the inside of the tube 2 is connected to a vacuum exhaust device 11 (maximum vacuum pressure I Xl0-'torr). .
本実施例では、泡を含む液は液入口4から容器1内へ入
り、複数のチューブ2のまわりを流れて液出口5から流
出する。各チューブ2内は真空排気装置11によって、
減圧されているために、液に含まれている泡は、チュー
ブ2内外の圧力差によって多孔質の気液分膜製のチュー
ブ2を通過してチューブ2内に入るが、液はその表面張
力によって多孔質疏水性の気液分離膜を通過することが
できず、気液の分離が行なわれる。In this embodiment, the liquid containing bubbles enters the container 1 through the liquid inlet 4, flows around the plurality of tubes 2, and flows out through the liquid outlet 5. The inside of each tube 2 is vacuum-exhausted by a vacuum exhaust device 11.
Due to the reduced pressure, the bubbles contained in the liquid pass through the porous gas-liquid membrane tube 2 and enter the tube 2 due to the pressure difference between the inside and outside of the tube 2, but the liquid's surface tension Therefore, the gas cannot pass through the porous hydrophobic gas-liquid separation membrane, and gas-liquid separation is performed.
以上の通り、本実施例においては、容器1内に液の流れ
に直角に複数のチューブ2を配置しているために、液中
の泡3がチューブ2に接触する頻度が高く、大量の液に
対して効果的な気液分離を行なうことができる。As described above, in this embodiment, since a plurality of tubes 2 are arranged in the container 1 at right angles to the flow of the liquid, the bubbles 3 in the liquid come into contact with the tubes 2 frequently, and a large amount of liquid Effective gas-liquid separation can be carried out.
また、宇宙空間等の微小重力空間においては、泡は液中
にランダムに混入しているために、各チューブ2によっ
て液より分離されること\なり、本実施例は微小重力空
間用として特に通している2なお、前記実施例では、複
数のチューブ2を、水平に、かつ液の流れに直角に配置
しているが、本発明においては、これを垂直方向、その
油液の流れを横切る任意の方向に配置することができる
。In addition, in a microgravity space such as outer space, bubbles are randomly mixed in the liquid, so they are separated from the liquid by each tube 2, so this embodiment is especially suitable for microgravity spaces. 2 In the above embodiment, the plurality of tubes 2 are arranged horizontally and perpendicular to the flow of the oil, but in the present invention, the tubes 2 are arranged vertically and at any arbitrary angle across the flow of the oil. It can be placed in the direction of
本発明では、容器内に液の流れを横切って複数の多孔質
の気液分離膜製チューブを配置し、同チューブ内を減圧
するこ々によって、容器内を流れる液中の泡がチューブ
に接触する頻度が高くなり、気液の分離効率を向上させ
ることができ、またこれに伴って、小型の装置で多量の
液の気液分離を行なうことができる。In the present invention, a plurality of porous gas-liquid separation membrane tubes are arranged in a container across the flow of liquid, and by reducing the pressure inside the tubes, bubbles in the liquid flowing in the container come into contact with the tubes. This increases the frequency of separation of gas and liquid, improving the efficiency of gas-liquid separation, and in conjunction with this, it is possible to perform gas-liquid separation of a large amount of liquid with a small-sized device.
第1図は本発明の一実施例に係る脱泡装置の全体ブロン
ク図、第2図は同実施例の脱泡部の断面図、第3図は従
来の平膜式脱泡装置の断面図である。
■・・・容器、 2・・・チューブ。
5・・・液出口
IO・・・脱泡部
11・・・真空排気装置。Fig. 1 is an overall brochure diagram of a defoaming device according to an embodiment of the present invention, Fig. 2 is a sectional view of the defoaming section of the same embodiment, and Fig. 3 is a sectional view of a conventional flat membrane defoaming device. It is. ■... Container, 2... Tube. 5...Liquid outlet IO...Defoaming section 11...Evacuation device.
Claims (1)
て配置された複数の多孔質の気液分離膜製のチューブ、
及び同チューブ内を減圧する排気装置を備えたことを特
徴とする脱泡装置。A container in which a liquid containing bubbles flows, a plurality of tubes made of a porous gas-liquid separation membrane arranged across the flow of the liquid in the container,
and a defoaming device comprising an exhaust device for reducing the pressure inside the tube.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10044590A JPH044002A (en) | 1990-04-18 | 1990-04-18 | Defoaming device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10044590A JPH044002A (en) | 1990-04-18 | 1990-04-18 | Defoaming device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH044002A true JPH044002A (en) | 1992-01-08 |
Family
ID=14274125
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10044590A Pending JPH044002A (en) | 1990-04-18 | 1990-04-18 | Defoaming device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH044002A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6402810B1 (en) * | 1997-04-23 | 2002-06-11 | Daimlerchrysler Ag | Method for dehydrating and/or degassing hydraulic fluids, device for carrying out said method and use of said device |
US6596058B2 (en) * | 2001-07-16 | 2003-07-22 | Systec, Inc. | Film degassing system |
US7022157B2 (en) * | 2003-11-12 | 2006-04-04 | Agilent Technologies, Inc. | Devices and methods for performing array based assays |
-
1990
- 1990-04-18 JP JP10044590A patent/JPH044002A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6402810B1 (en) * | 1997-04-23 | 2002-06-11 | Daimlerchrysler Ag | Method for dehydrating and/or degassing hydraulic fluids, device for carrying out said method and use of said device |
US6596058B2 (en) * | 2001-07-16 | 2003-07-22 | Systec, Inc. | Film degassing system |
US7022157B2 (en) * | 2003-11-12 | 2006-04-04 | Agilent Technologies, Inc. | Devices and methods for performing array based assays |
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