JPS6048104A - Defoaming process and apparatus - Google Patents
Defoaming process and apparatusInfo
- Publication number
- JPS6048104A JPS6048104A JP58155805A JP15580583A JPS6048104A JP S6048104 A JPS6048104 A JP S6048104A JP 58155805 A JP58155805 A JP 58155805A JP 15580583 A JP15580583 A JP 15580583A JP S6048104 A JPS6048104 A JP S6048104A
- Authority
- JP
- Japan
- Prior art keywords
- tube
- liquid
- defoaming
- pipe
- permeable porous
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0031—Degasification of liquids by filtration
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は液体中に含まれる気泡、特に除去に手間のかか
る微細な気泡を、その液体の管による輸送過程において
効率よく除去する脱泡装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a defoaming device that efficiently removes air bubbles contained in a liquid, particularly fine air bubbles that take time and effort to remove, during the process of transporting the liquid through a pipe.
従来より液体中の微細気泡を効率よく充分に除去するこ
との必要性は随所にある。例えば血管中への薬液の注入
、液体クロマトグラフの試薬の注入、キャスティング法
によるフィルム原液の送液等である。これらは微細の気
泡の存在も悪影響が大きいので、その徹底した除去が必
要である。長時間の静置或は減圧処理等でこれら微細気
泡の除去は可能であるが、このような処理が輸液工程中
に入ることは繁雑である。特に連続輸液工程中で脱泡の
必要がある場合には、輸液管の中で短時間に効率よ除去
することが望まれる。更に連続輸液管の前に接続する攪
拌工程があったり、ポンプがあったりする場合には気泡
の混入する機会も一層多く、それ丘゛1す迅速で効率の
よい脱泡が望まれる。。Conventionally, there has been a need to efficiently and sufficiently remove microbubbles in liquids. Examples include injection of a drug solution into a blood vessel, injection of a reagent for liquid chromatography, and delivery of a film stock solution by a casting method. Since the presence of fine bubbles has a large negative effect on these, it is necessary to thoroughly remove them. Although it is possible to remove these microbubbles by allowing the solution to stand still for a long time or by reducing the pressure, it is complicated to perform such a process during the infusion process. Particularly when defoaming is required during a continuous infusion process, it is desirable to remove bubbles efficiently in a short time in the infusion tube. Furthermore, if there is a stirring process or a pump connected in front of the continuous infusion pipe, there is an even greater chance of air bubbles being mixed in, so rapid and efficient defoaming is desired. .
然るに従来このような気泡を特に輸液管を通る間に充分
に効率よく除く方法はなかった。However, until now, there has been no method for sufficiently efficiently removing such air bubbles, particularly during passage through an infusion tube.
本発明者等はこのような要望を充たす方法について種々
検討の結果本廃明に到達したものである。The inventors of the present invention have arrived at the present invention as a result of various studies on methods to satisfy such demands.
即ち本発明は対象となる液体に対して不透過性の通気性
多孔質体より成る管を用い、該液体中に含まれる気泡を
、該液体が該連続多孔質体管を通過する間に肢管の管壁
を通して除去するものである。That is, the present invention uses a tube made of an air-permeable porous material that is impermeable to the target liquid, and removes air bubbles contained in the liquid while the liquid passes through the continuous porous tube. It is removed through the wall of the tube.
任意の液体が通気性多孔質体に対して不透過であるため
には、該液体が該通気性多孔質体を構成する物質に対す
る接触角で90度以上であることが必要である。このよ
うな組合せとしては、例えば液体が水の場合、ポリテト
ラフルオロエチレン、ポリプロピレン、ポリエチレン等
との組合せがある。In order for any liquid to be impermeable to the breathable porous body, it is necessary that the liquid has a contact angle of 90 degrees or more with respect to the substance constituting the breathable porous body. Examples of such combinations include, when the liquid is water, combinations with polytetrafluoroethylene, polypropylene, polyethylene, etc.
このように輸液管に液が流れる間に気泡が輸液管壁を通
って管外に除かれるためには、通気性多孔質体の管内の
気泡圧が管外の圧力よりも高いことが必要であり、この
圧力差が大きい程効率がよい。従って管外気圧を大気圧
以下に減圧することも有効である。なお管内圧が余りに
高くなると、本来この材質の通気性多孔質体に対して不
透過性の液体であっても遂に連続気孔を通って透過する
ようになる。この限界圧は連続気孔が小さくなる程高く
なる。従ってこの液漏れを生じない範囲で管内圧を高く
、且つ管壁の連続気孔を大きく、管壁の空隙率を高く、
更に多孔質管壁の厚さをうすくする程脱泡効率はよくな
る。一般に輸液管中の圧が低い場合には脱泡に充分な圧
が得られない場合があるが、この場合には脱泡部の管中
の圧を必要な水準迄高める工夫が必要である。これは脱
泡用通気性多孔質管からの流出管径が、肢管への流入管
径よりも細くすることで有効に達せられる。In order for air bubbles to pass through the walls of the infusion tube and be removed from the infusion tube while the liquid is flowing through the infusion tube, the bubble pressure inside the tube made of breathable porous material must be higher than the pressure outside the tube. The larger the pressure difference, the better the efficiency. Therefore, it is also effective to reduce the pressure outside the tube to below atmospheric pressure. Note that if the internal pressure of the tube becomes too high, even a liquid that is originally impermeable to the air-permeable porous body made of this material will eventually permeate through the continuous pores. This critical pressure becomes higher as the continuous pores become smaller. Therefore, the internal pressure of the pipe is increased within a range that does not cause this liquid leakage, the continuous pores of the pipe wall are made large, the porosity of the pipe wall is increased,
Furthermore, the thinner the porous tube wall is, the better the defoaming efficiency becomes. Generally, when the pressure in the infusion tube is low, sufficient pressure may not be obtained for defoaming, but in this case, it is necessary to take measures to increase the pressure in the tube of the defoaming section to the required level. This can be effectively achieved by making the diameter of the outflow pipe from the air-permeable porous defoaming pipe smaller than the diameter of the inflow pipe to the limb canal.
これは脱泡用管が、脱泡用液体の入口から出口に向う方
向に次第に細くなるようにテーパーをつけることによっ
ても達せられる。また流出管の先端に絞り装置を取付け
、これによって流出管の流出断面積を調節することによ
っても達せられる。This can also be achieved by tapering the defoaming tube so that it becomes narrower in the direction from the inlet to the outlet of the defoaming liquid. This can also be achieved by attaching a throttling device to the tip of the outflow pipe, thereby adjusting the outflow cross-sectional area of the outflow pipe.
なお通気性多孔質管の厚さは薄い方が脱泡効率がよいが
、余蛛薄いと強度的に問題がある。この場合には通気抵
抗が殆んどない補強用の多孔質層を積層させることが望
ましい。また管径については細い方が脱泡効率を高める
上からは好ましい。Note that the thinner the breathable porous tube is, the better the defoaming efficiency is, but if it is too thin, there will be problems in terms of strength. In this case, it is desirable to laminate a reinforcing porous layer with almost no ventilation resistance. Further, as for the pipe diameter, a smaller one is preferable from the viewpoint of improving the defoaming efficiency.
更に脱泡の対象となる液体が溶液である場合には、長時
間の使用に際し、脱泡用通気性多孔質管の管壁の通気孔
が溶媒の蒸発に伴なって溶質によって閉塞されることが
ある。このような場合には通気性多孔質管使用の脱泡部
を溶液の溶剤中に浸漬して溶質の析出による閉塞を防止
することが有効である。Furthermore, when the liquid to be degassed is a solution, the vent holes in the tube wall of the ventilated porous tube for defoaming may become clogged with solute due to evaporation of the solvent during long-term use. There is. In such cases, it is effective to immerse a defoaming section using an air-permeable porous tube in the solvent of the solution to prevent blockage due to solute precipitation.
本脱泡装置の代表的な実施の態様を図1.2.3に示し
た。図3に示すものを例にとって本発明の詳細な説明す
る。流入側輸液管1を通って微細な気泡6を含んだ気泡
含有液4が送られてくる。これは脱泡用通気性多孔質管
2より成る脱泡部を通るが、この圧は流出側輸液管3の
先端に取付けられた絞り装置7の絞りを調節して、必要
流量を確保した上で、脱泡に必要な水準に設定される。A typical embodiment of this defoaming device is shown in Figure 1.2.3. The present invention will be described in detail by taking the example shown in FIG. 3 as an example. A bubble-containing liquid 4 containing fine bubbles 6 is sent through the inflow side infusion pipe 1. This passes through a defoaming section consisting of an air-permeable porous defoaming tube 2, but this pressure is adjusted by adjusting the throttle of the throttle device 7 attached to the tip of the outflow side infusion tube 3 to ensure the required flow rate. The level is set to the level required for defoaming.
かくして液甲の気泡は脱泡部を通る間に、脱泡用通気性
多孔質管2の管壁の通気孔を通って管外に除去される。Thus, while the bubbles in the liquid shell pass through the defoaming section, they are removed to the outside of the tube through the vents in the tube wall of the ventilated porous tube 2 for defoaming.
かくして気泡除去液5は流出側輸液管3を通って次の工
程に送られる。図1は脱泡部に必要な加圧を流入側輸液
管1の内径よりも小さい内径の流出側輸液管を用いて行
なうものである。また図2はこの加圧を脱泡用液体の入
口から出口に向う方向に次第に細くなるテーパーのつい
た脱泡用通気性多孔質管を用いて行なうものである。The bubble removing liquid 5 is thus sent to the next step through the outflow side infusion pipe 3. In FIG. 1, the pressure necessary for the defoaming section is applied using an outflow infusion tube having an inner diameter smaller than that of the inflow infusion tube 1. Further, in FIG. 2, this pressurization is performed using a gas-permeable porous pipe for defoaming which has a taper that becomes gradually thinner in the direction from the inlet to the outlet of the defoaming liquid.
本脱泡装置に用いる通気性多孔質体として特に有効なも
のの一つとして図4に示すような、多数の結節8と、こ
れを結びつける無数のフィブリル9とより成る延伸多孔
質ポリテトラフルオロエチレンがある。これは例えば特
公昭51−18991に詳述されているような方法によ
ってつくることができる。これは水に対する接触角10
8度で、水或は水系溶液には不透過性のためこれよりの
脱泡に対して特に有効である。One of the particularly effective breathable porous materials used in this defoaming device is stretched porous polytetrafluoroethylene, which is composed of a large number of nodules 8 and countless fibrils 9 that connect them, as shown in FIG. be. This can be produced, for example, by a method as detailed in Japanese Patent Publication No. 51-18991. This is the contact angle to water of 10
8 degrees and is impermeable to water or aqueous solutions, making it particularly effective for defoaming.
以下実施例について説明する。Examples will be described below.
図1に示すような構成で内径o、 3 tar 、外径
2圏の7リコンチユーブを通して、微細気泡の混入した
水を輸送し、この流出側に長さ40++II+1の延伸
多孔質ポリテトラフルオロエチレンチューブを接続した
。これは長さ方向にフィブリルが配列し、これと直角方
向に結節の長手方向が配列し、結節が多くのフィブリル
によって連結された構造のもので、ボアテックスチュー
ブとして知られているものである。このものの物性は次
の通りである。With the configuration shown in Figure 1, water mixed with microbubbles is transported through 7 recontubes with an inner diameter of 3 tar and an outer diameter of 2, and a stretched porous polytetrafluoroethylene tube with a length of 40++II+1 is placed on the outflow side. Connected. This tube has a structure in which fibrils are arranged in the longitudinal direction, nodes are arranged in the longitudinal direction at right angles to this, and the nodes are connected by many fibrils, and is known as a Voretex tube. The physical properties of this material are as follows.
内 径 2.0 ■
肉 厚 04調
空隙率 50チ
侵水圧 0.9 Ky/cr1
次いでボアテックスチューブの先に内径0.2叫、外径
2諭のシリコンチューブを接続し、ボアテックスチュー
ブの流路長が30+++mになるようにした。Inner diameter 2.0 ■ Wall thickness 04 Porosity 50 Invasion pressure 0.9 Ky/cr1 Next, connect a silicone tube with an inner diameter of 0.2 mm and an outer diameter of 2 to the tip of the Vore Tex tube, and The length of the flow path was set to 30 +++ m.
ボアテックスチューブを通る間に水中の微細気泡は完全
に除去され、内径0.2 mmのプリコンチューブから
流出する水には気泡は全く認められなかった。Microbubbles in the water were completely removed while passing through the Voretex tube, and no air bubbles were observed in the water flowing out from the precon tube with an inner diameter of 0.2 mm.
図1は本発明による実施態様の一つを示す概略図である
。図の数字は次の通りである。
1・・・流入側輸液管、2・・・脱泡用通気性多孔質管
、3・・流出側輸液管、4・・・気泡含有液、5・・・
気泡除去液、 6・・気泡、
7・・絞り装置、8・・・結節、
9・・・フィブリル。
図2は本発明による実施態様の他の一つを示す概略図で
ある。
図3は本発明による実施態様の他の一つを示す概略図で
ある。
図4は本装置に用いる脱泡用チューブに適したポリテト
ラフルオロエチレンの延伸多孔質体の微細構造を示す図
である。FIG. 1 is a schematic diagram showing one embodiment according to the invention. The numbers in the figure are as follows. DESCRIPTION OF SYMBOLS 1...Inflow side infusion pipe, 2...Air permeable porous pipe for defoaming, 3...Outflow side infusion pipe, 4...Bubble-containing liquid, 5...
Air bubble removal liquid, 6. Air bubbles, 7. Squeezing device, 8. Nodules, 9. Fibrils. FIG. 2 is a schematic diagram showing another embodiment according to the present invention. FIG. 3 is a schematic diagram showing another embodiment according to the present invention. FIG. 4 is a diagram showing the fine structure of a stretched porous body of polytetrafluoroethylene suitable for a defoaming tube used in this device.
Claims (1)
成る管を用い、該液体中に含まれる気泡を、該液体が該
連続多孔質体管を通過する間に、該管の管壁を通して除
去することを特徴とする脱泡方法。 2、脱泡用通気性多孔質管内の気泡含有流体静圧が、管
外圧力よりも高くなるように構成されたことを特徴とす
る特許請求り範囲1.に記載の脱泡方法。 3、脱泡用通気性多孔質管からの流出管径を、該管への
流入管径よりも細くすることによって、該管内圧を高め
ることを特徴とする特許請求の範囲1.2.に記載の脱
泡方法。 4、脱泡用管を構成する通気性多孔質体が連続気孔性ポ
リテトラフルオロエチレン或いは同ポリプロピレン又は
ポリエチレンの倒れかであることを特徴とする特許請求
の範囲1.2.3.に記載の脱泡方法を実施するための
装置。 5、脱泡用管の管壁が二層以上から構成されており、そ
の中の少なくとも一層が特許請求の範囲1゜4、5.6
.に記載の通気性多孔質体であり、該管壁が全体として
通気性であることを特徴とする特許請求の範囲1.2.
3.記載の脱泡方法を実施するだめの装置。[Claims] 1. Using a tube made of an air-permeable porous material that is impermeable to any liquid, the liquid passes through the continuous porous material tube to remove air bubbles contained in the liquid. A defoaming method characterized in that the degassing is carried out through the pipe wall of the pipe. 2. Claim 1, characterized in that the static pressure of the bubble-containing fluid within the air-permeable porous tube for defoaming is configured to be higher than the pressure outside the tube. Defoaming method described in. 3. Claim 1.2, characterized in that the pressure inside the tube is increased by making the diameter of the outflow tube from the air-permeable porous tube for defoaming smaller than the diameter of the inflow tube into the tube. Defoaming method described in. 4. Claim 1.2.3. The breathable porous material constituting the defoaming tube is made of open-pore polytetrafluoroethylene, polypropylene, or polyethylene. An apparatus for carrying out the defoaming method described in . 5. The wall of the defoaming tube is composed of two or more layers, at least one of which is within the scope of claim 1.4, 5.6.
.. Claim 1.2. is a breathable porous body according to claim 1.2, characterized in that the tube wall is breathable as a whole.
3. A device for carrying out the degassing method described.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58155805A JPS6048104A (en) | 1983-08-26 | 1983-08-26 | Defoaming process and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58155805A JPS6048104A (en) | 1983-08-26 | 1983-08-26 | Defoaming process and apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6048104A true JPS6048104A (en) | 1985-03-15 |
Family
ID=15613834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58155805A Pending JPS6048104A (en) | 1983-08-26 | 1983-08-26 | Defoaming process and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6048104A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63111909A (en) * | 1986-10-30 | 1988-05-17 | Eruma:Kk | Degasification apparatus |
| JPS63158106A (en) * | 1986-12-22 | 1988-07-01 | Fuji Photo Film Co Ltd | Deaerating method |
| US4787921A (en) * | 1986-06-13 | 1988-11-29 | Japan Gore-Tex, Inc. | Degassing tube |
| JPH01224077A (en) * | 1988-03-01 | 1989-09-07 | Fuji Photo Film Co Ltd | Coating method |
| US4869732A (en) * | 1988-12-23 | 1989-09-26 | Texaco Inc. | Deoxygenation of aqueous polymer solutions used in enhanced oil recovery processes |
| US4985055A (en) * | 1988-12-19 | 1991-01-15 | The Boc Group, Inc. | Liquid/gas separation device |
| US4986837A (en) * | 1986-12-12 | 1991-01-22 | Yoshihiko Shibata | Apparatus for degassing a liquid |
| US5123937A (en) * | 1989-02-03 | 1992-06-23 | Japan Gore-Tex Inc. | Deaerating film and deaerating method |
| JP2017181110A (en) * | 2016-03-28 | 2017-10-05 | 積水メディカル株式会社 | Deaerator |
| WO2023007808A1 (en) * | 2021-07-26 | 2023-02-02 | ウシオ電機株式会社 | Liquid chromatograph and liquid sample analysis method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5331040U (en) * | 1976-08-24 | 1978-03-17 | ||
| JPS54123785A (en) * | 1978-02-24 | 1979-09-26 | Du Pont | Deaerator |
-
1983
- 1983-08-26 JP JP58155805A patent/JPS6048104A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5331040U (en) * | 1976-08-24 | 1978-03-17 | ||
| JPS54123785A (en) * | 1978-02-24 | 1979-09-26 | Du Pont | Deaerator |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4787921A (en) * | 1986-06-13 | 1988-11-29 | Japan Gore-Tex, Inc. | Degassing tube |
| JPS63111909A (en) * | 1986-10-30 | 1988-05-17 | Eruma:Kk | Degasification apparatus |
| US4986837A (en) * | 1986-12-12 | 1991-01-22 | Yoshihiko Shibata | Apparatus for degassing a liquid |
| JPS63158106A (en) * | 1986-12-22 | 1988-07-01 | Fuji Photo Film Co Ltd | Deaerating method |
| JPH01224077A (en) * | 1988-03-01 | 1989-09-07 | Fuji Photo Film Co Ltd | Coating method |
| US4985055A (en) * | 1988-12-19 | 1991-01-15 | The Boc Group, Inc. | Liquid/gas separation device |
| US4869732A (en) * | 1988-12-23 | 1989-09-26 | Texaco Inc. | Deoxygenation of aqueous polymer solutions used in enhanced oil recovery processes |
| US5123937A (en) * | 1989-02-03 | 1992-06-23 | Japan Gore-Tex Inc. | Deaerating film and deaerating method |
| JP2017181110A (en) * | 2016-03-28 | 2017-10-05 | 積水メディカル株式会社 | Deaerator |
| WO2023007808A1 (en) * | 2021-07-26 | 2023-02-02 | ウシオ電機株式会社 | Liquid chromatograph and liquid sample analysis method |
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