JPH1147508A - Defoaming method - Google Patents

Defoaming method

Info

Publication number
JPH1147508A
JPH1147508A JP20661197A JP20661197A JPH1147508A JP H1147508 A JPH1147508 A JP H1147508A JP 20661197 A JP20661197 A JP 20661197A JP 20661197 A JP20661197 A JP 20661197A JP H1147508 A JPH1147508 A JP H1147508A
Authority
JP
Japan
Prior art keywords
liquid
foam
bubbles
containing liquid
degassing
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.)
Granted
Application number
JP20661197A
Other languages
Japanese (ja)
Other versions
JP3729374B2 (en
Inventor
Toru Onogawa
徹 小野川
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP20661197A priority Critical patent/JP3729374B2/en
Publication of JPH1147508A publication Critical patent/JPH1147508A/en
Application granted granted Critical
Publication of JP3729374B2 publication Critical patent/JP3729374B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently and completely remove even fine foams within a short time independently of the viscosity of a foam-containing liquid body by degassing the foam-containing liquid and then capturing the foams. SOLUTION: A liquid 3 to be adjusted by being stirred and mixed by a mixing apparatus 2 in a liquid adjustment tank 1 contains large and small foams 4. The foam-containing liquid body 3 is sent to a defoaming apparatus 5 through a liquid sending pipe 10 by a liquid sending pump 11. The defoaming apparatus 5 is constituted of a degassing apparatus 6 and a filtering apparatus 7 and the foam-containing liquid body 3 is at first sent to the degassing apparatus 6. The degassing apparatus 6 is for decreasing the dissolved air amount in the foam-containing coating liquid 3 and mainly removes large foams in the liquid and carries out treatment to provide tolerance of air dissolving performance of the liquid. The foam-containing liquid 3 is then sent to the filtering apparatus 7. The filtering apparatus 7 captures fine foams in the foam- containing liquid body 3 which are not removed by the degassing treatment by the degassing apparatus 6 on the surface of a filter medium and removes the foams by dissolving them in the liquid.

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、気泡を含有する含
泡液体から液中の気泡を取り除く脱泡方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a defoaming method for removing bubbles in a liquid from a bubble-containing liquid containing bubbles.

【0002】[0002]

【従来の技術】例えば写真用感光材料、感光性印刷版材
料、磁性材料等の各種記録材料用塗工液は、調製時に攪
拌混合されるため、液中に多量の気泡を含んでおり、そ
のまま使用すると塗膜にピンホールやスジ状のむら等が
出来てしまう。そのため、塗工液は液中の気泡を取り除
いてから使用される。
2. Description of the Related Art For example, coating liquids for various recording materials such as photographic light-sensitive materials, photosensitive printing plate materials, and magnetic materials are stirred and mixed at the time of preparation, and therefore contain a large amount of bubbles in the liquid. If it is used, pinholes or streak-like unevenness are formed on the coating film. Therefore, the coating liquid is used after removing bubbles in the liquid.

【0003】このような含泡液体中の気泡を除去するた
め、従来より、気泡と液との質量差を利用して脱泡槽内
に所定時間静置したり、特殊な流路が形成された脱泡槽
内を通過させたりして気泡を液面に浮上させ、この浮上
した気泡が自然に壊れるのを待って脱泡する方法(例え
ば、特開昭56−97508号公報)、前記の方法に更
に脱泡槽内を真空排気して脱泡効率を向上させる方法
(例えば、特開昭56−100610号公報)、また脱
泡槽内に超音波振動を与えて気泡を破泡する方法(例え
ば、特公昭47−6835号公報)等が知られている。
[0003] In order to remove such bubbles in the foam-containing liquid, a conventional method has been employed in which a difference in mass between the bubbles and the liquid is used to allow the bubble to remain in a defoaming tank for a predetermined time or a special flow path is formed. A bubble is floated on the liquid surface by passing through the inside of a defoaming tank, and defoaming after the floated bubble is naturally broken (for example, JP-A-56-97508). In addition to the method, a method for improving the defoaming efficiency by evacuating the inside of the defoaming tank (for example, JP-A-56-100610), and a method for breaking bubbles by applying ultrasonic vibration to the defoaming tank (For example, Japanese Patent Publication No. 47-6835) and the like.

【0004】[0004]

【発明が解決しようとする課題】しかしながら従来の脱
泡方法において、質量差による脱泡方法では、含有液体
の粘度が高くなると、気泡の浮上に長時間を要し、特に
気泡が小さくなるほど浮上し難くなる。この点に関し
て、真空排気を付加することによりある程度改善される
ものの、液中の微小な気泡まで完全に除去するには槽内
の真空度をかなり高める必要がある。また、含泡液体の
処理量に応じて脱泡槽も大きくしなければならず、装置
が大型化するという欠点もある。
However, in the conventional defoaming method, in the defoaming method based on the difference in mass, when the viscosity of the contained liquid becomes high, it takes a long time for air bubbles to float. It becomes difficult. In this regard, although the degree of improvement can be improved to some extent by adding vacuum evacuation, it is necessary to considerably increase the degree of vacuum in the tank in order to completely remove even minute bubbles in the liquid. In addition, the size of the defoaming tank must be increased in accordance with the processing amount of the foam-containing liquid, and there is a disadvantage that the apparatus becomes large.

【0005】超音波による方法では、超音波発生手段
(超音波振動子等)を駆動するための高出力電気設備を
要するために、爆発性気体雰囲気、即ち防爆箇所には適
用できず、また超音波の振動により装置自体が劣化した
り、場合によっては破損するおそれがある。更に、超音
波発生手段を必要とするため、他の方法に比べて装置が
高価であるという欠点もある。
[0005] In the method using ultrasonic waves, high-output electrical equipment for driving ultrasonic generating means (ultrasonic vibrator or the like) is required, so that it cannot be applied to an explosive gas atmosphere, that is, an explosion-proof place. The device itself may be degraded or damaged in some cases by the vibration of the sound waves. Further, there is a disadvantage that the apparatus is more expensive than other methods because of the need for the ultrasonic wave generating means.

【0006】本発明は前記したような従来技術の欠点を
解消し、含泡液体の粘度が数cpと低い場合は勿論、数
100cpと非常に高い場合でも、短時間で微小な気泡
まで完全に脱泡でき、しかも安価で、適用箇所の制約も
無い脱泡方法を提供することを目的とする。
The present invention solves the above-mentioned drawbacks of the prior art. Even when the viscosity of the bubble-containing liquid is as low as several cp or as high as several hundred cp, it is possible to completely remove small bubbles in a short time. It is an object of the present invention to provide a defoaming method which can be defoamed, is inexpensive, and has no restriction on an application place.

【0007】[0007]

【課題を解決するための手段】本発明者らは、上記の目
的を達成するために鋭意研究を重ねた結果、塗工液を脱
気処理した後に濾過することにより、高粘度の塗工液で
も短時間で、しかも微小な気泡まで完全に除去できるこ
とを見い出し、本発明を完成するに至った。即ち、上記
の目的は、本発明の、含泡液体中の気泡を取り除く脱泡
方法において、前記含泡液体を脱気処理した後、気泡を
捕獲することを特徴とする脱泡方法により達成される。
上記脱泡方法によれば、脱気処理により、液の空気溶解
能力に十分な余裕を与え、しかる後濾過することによ
り、使用濾材の目開きよりも大きな直径の気泡を完全に
除去する。従って、脱気度及び濾材の目開きの設定によ
り、含泡液体の粘度に係わらず、短時間で効率よく、微
小な気泡まで完全に除去することができる。しかも、処
理に際して超音波発生器のような高価で、高出力を要す
る装置を必要としないため、安価に、また設置箇所の制
限を受けることもなく、含泡液体の脱泡を行うことがで
きる。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to achieve the above object, and as a result, by filtering a coating solution after deaeration, the coating solution having a high viscosity has been obtained. However, they have found that even minute bubbles can be completely removed in a short time, and have completed the present invention. That is, the above object is achieved by a defoaming method of the present invention for removing bubbles in a foam-containing liquid, which comprises degassing the foam-containing liquid and then capturing the bubbles. You.
According to the above defoaming method, a sufficient margin is given to the air dissolving ability of the liquid by the deaeration treatment, and thereafter, by filtering, the bubbles having a diameter larger than the aperture of the filter medium to be used are completely removed. Therefore, by setting the degree of deaeration and the aperture of the filter medium, small bubbles can be completely and efficiently removed in a short time regardless of the viscosity of the bubble-containing liquid. Moreover, since expensive and high-powered devices such as an ultrasonic generator are not required for the treatment, the defoaming of the foam-containing liquid can be performed at low cost and without restriction on the installation location. .

【0008】[0008]

【発明の実施の形態】本発明の脱泡方法について、図面
を参照して詳細に説明する。図1は、本発明の脱泡方法
を実施するための装置構成を示す模式図である。図示さ
れるように、液調合タンク1内では、原料となる各種添
加剤と溶剤とを攪拌機2で攪拌混合して調製される液3
は、攪拌混合に伴い巻き込まれた空気からなる大小の気
泡4を多量に含んでいる。以下、この液を含泡液体と呼
ぶ。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The defoaming method of the present invention will be described in detail with reference to the drawings. FIG. 1 is a schematic diagram showing an apparatus configuration for performing the defoaming method of the present invention. As shown in the drawing, in a liquid preparation tank 1, a liquid 3 prepared by stirring and mixing various additives as a raw material and a solvent with a stirrer 2 is used.
Contains a large amount of large and small bubbles 4 composed of air entrained by stirring and mixing. Hereinafter, this liquid is referred to as a bubble-containing liquid.

【0009】この含泡液体3は、送液管10を通じて送
液ポンプ11により脱泡装置5に送られる。脱泡装置5
は脱気装置6と濾過装置7とで構成されており、含泡液
体3は先ず脱気装置6へと送られる。脱気装置6は、含
泡塗工液3中の溶存空気量を下げるための装置であり、
主として液中の比較的大きな気泡を取り除き、液の空気
溶解能力に余裕を持たせるための処理を行う。この脱気
の手法として、例えば、真空装置を連結して槽内を減圧
する方法がある。減圧により溶存空気を析出させ、かつ
液中での気泡の浮上を促進し、更に液面に到達した気泡
を強制的に破泡することで、含泡液体3の溶存空気量を
短時間で低下させるとができる。この時の減圧の程度
は、従来の真空排気による方法のように気泡を完全に除
去する目的ではないために特に高い真空度は必要はな
く、含泡塗工液3の粘度や後述される脱気の程度にもよ
るが、概ね数十torr程度の真空度で十分である。ま
た、脱気手段として気液分離膜を用いることも可能であ
る。その他、液中の溶存空気量を下げ得る方法であれば
特に制限されることなく用いることができる。この脱気
装置6による脱気処理は、含泡塗工液3の飽和溶存空気
量の90%以下、好ましくは80%以下の脱気度になる
まで行うことが望ましい。これにより、次段の濾過装置
7による処理を効率よく行うことができる。
The bubble-containing liquid 3 is sent to a defoaming device 5 by a liquid sending pump 11 through a liquid sending pipe 10. Defoaming device 5
Is composed of a deaerator 6 and a filter 7, and the bubble-containing liquid 3 is first sent to the deaerator 6. The deaerator 6 is a device for reducing the amount of dissolved air in the foamed coating liquid 3,
A process is mainly performed to remove relatively large bubbles in the liquid and to allow the liquid to dissolve in air. As a method of this deaeration, for example, there is a method of connecting a vacuum device to reduce the pressure in the tank. Dissolved air is precipitated by depressurization, the floating of bubbles in the liquid is promoted, and the bubbles reaching the liquid level are forcibly broken to reduce the dissolved air amount of the bubble-containing liquid 3 in a short time. It can be done. The degree of pressure reduction at this time does not need to be particularly high, since it is not the purpose of completely removing air bubbles unlike the conventional method using vacuum evacuation, and the degree of pressure reduction is not necessary. Although it depends on the degree of mind, a degree of vacuum of about several tens torr is sufficient. Further, it is also possible to use a gas-liquid separation membrane as the degassing means. In addition, any method can be used without particular limitation as long as it can reduce the amount of dissolved air in the liquid. The deaeration treatment by the deaerator 6 is desirably performed until the deaeration of the bubble-containing coating liquid 3 becomes 90% or less, preferably 80% or less of the saturated dissolved air amount. Thereby, the processing by the filtration device 7 at the next stage can be efficiently performed.

【0010】含泡液体3は、次いで濾過装置7に送られ
る。この濾過装置7は、脱気装置6での脱気処理によっ
て除去されなかった含泡液体3中の微小な気泡を濾材表
面で捕獲し、液中に溶解せしめることで除去するための
装置であり、例えば合成樹脂製の不織布や金網、金属焼
結体、セラミックス製多孔体等からなる濾材を備える。
含泡液体3中の気泡は、濾材を通過する際に、濾材の開
口部と接触して破泡したり、更に小さな気泡に分割され
る。従って、濾材の目開きは脱泡目的とする気泡の直径
よりも小さな隙間とする必要がある。使用する濾材の目
開きは塗工液の種類、用途により適宜選択される。例え
ば写真用感光材料や磁気記録媒体用磁性塗料等のように
サブミクロンオーダーの薄層に塗布され、しかも均質な
塗膜が要求される場合には、塗膜に極く微細なピンホー
ルやむらが発生してもその製品価値を著しく低下するた
めに、目開きとして3μmメッシュ以下の目の細かい濾
材を用いて直径3μm以下の気泡まで完全に除去する。
また、活字を形成するような印刷インク等では、写真用
感光材料や磁気記録媒体用磁性塗料のような完全脱泡は
要求されず、30μmメッシュ程度のやや粗い目開きの
濾材を使用することもできる。このように、濾過装置7
においては、脱泡目的とする気泡の直径よりも小さな目
開きの濾材を使用することが重要である。
[0010] The bubble-containing liquid 3 is then sent to a filtration device 7. The filtering device 7 is a device for capturing fine bubbles in the bubble-containing liquid 3 that have not been removed by the degassing process in the degassing device 6 on the surface of the filter medium and dissolving them in the liquid to remove them. For example, a filter medium made of a synthetic resin nonwoven fabric, a wire mesh, a metal sintered body, a ceramic porous body, or the like is provided.
When passing through the filter medium, the bubbles in the bubble-containing liquid 3 come into contact with the openings of the filter medium and break or break up into smaller bubbles. Therefore, the openings of the filter medium must be smaller than the diameter of the bubble to be defoamed. The aperture of the filter medium to be used is appropriately selected depending on the type and application of the coating liquid. For example, when a thin film of submicron order is applied such as a photographic light-sensitive material or a magnetic paint for a magnetic recording medium and a uniform coating is required, extremely fine pinholes and unevenness are required in the coating. Even if 著 し く occurs, the product value is significantly reduced. Therefore, air bubbles having a diameter of 3 µm or less are completely removed by using a fine filter medium having a mesh of 3 µm or less as openings.
In the case of printing ink or the like that forms type, complete defoaming is not required as in the case of photographic photosensitive materials or magnetic paints for magnetic recording media, and it is also possible to use a filter medium having a coarse opening of about 30 μm mesh. it can. Thus, the filtering device 7
In the above, it is important to use a filter medium having an opening smaller than the diameter of the bubble to be defoamed.

【0011】この濾過装置7による処理速度は、使用す
る濾材の種類や濾過面積、含泡液体3の粘度や種類等に
より異なり、適宜設定される。尚、実際の処理に際し
て、濾材は予め塗工液と同一の液中に浸漬し、濾材内部
の空気を抜いておくことが望ましい。また、この濾過処
理では、気泡の除去とともに、含泡液体3に含まれる不
純物や不溶解物を同時に取り除くことができるという利
点も有する。
The processing speed of the filtration device 7 varies depending on the type and filtering area of the filter medium to be used, the viscosity and type of the bubble-containing liquid 3, and the like, and is appropriately set. At the time of the actual treatment, it is desirable that the filter medium is immersed in the same liquid as the coating liquid in advance and the air inside the filter medium is evacuated. In addition, this filtration treatment has an advantage that impurities and insolubles contained in the bubble-containing liquid 3 can be removed simultaneously with the removal of bubbles.

【0012】そして、上記の如く脱泡装置5での脱泡処
理によって気泡が完全に取り除かれた脱泡液9は、貯液
タンク8に貯蔵されるか、図示されない塗布工程へと連
続して送られる。
The defoaming liquid 9 from which bubbles have been completely removed by the defoaming treatment in the defoaming device 5 as described above is stored in the storage tank 8 or continuously to a coating step (not shown). Sent.

【0013】以下、本発明の脱泡方法に関して実施例を
挙げて更に明確にする。 (実施例1〜2及び比較例1〜2)9重量%のポリビニ
ルアルコール(PVA)水溶液を、攪拌機を用いて調製
した。このPVA水溶液は液中に大小の気泡を多量に含
んでおり、また粘度を測定したところ、39cpであっ
た。そして、このPVA水溶液を図1に示す脱泡装置に
従い処理した。先ず、PVA水溶液を脱気処理した。こ
の脱気処理は、ジャパンゴアテックス(株)製「DMS
−1F」を用いて40torrの真空度に減圧し、PV
A水溶液の溶存空気量が1.5ppm(脱気度20%相
当)となるように処理した。次いで、濾過処理を行っ
た。この濾過処理は、日本ポール(株)製「NMS01
−L1 G16H」を用いて、ポリプロピレン製不織布か
らなり、濾過面積510cm2 で、目開き3μm(実施
例1)及び30μmメッシュ(実施例2)の濾材を装填
して、液流量1リットル/分で行った。尚、濾材は予め
PVA水溶液中に浸漬して、内部の空気を抜いておい
た。上記の各処理を行ったPVA水溶液中に残存する気
泡の数を、超音波式気泡検出計により計測した。計測結
果として、直径30μm以上の気泡と同30μm以下の
気泡とに分類し、それぞれの残存数を表1に示す。
Hereinafter, the defoaming method of the present invention will be further clarified by giving examples. (Examples 1 and 2 and Comparative Examples 1 and 2) A 9% by weight aqueous solution of polyvinyl alcohol (PVA) was prepared using a stirrer. This PVA aqueous solution contained a large amount of large and small bubbles in the liquid, and the viscosity was measured to be 39 cp. Then, this PVA aqueous solution was treated according to the defoaming apparatus shown in FIG. First, the PVA aqueous solution was degassed. This degassing process is performed by "DMS" manufactured by Japan Gore-Tex Corporation.
-1F "to a vacuum of 40 torr,
The aqueous solution A was treated so that the dissolved air amount was 1.5 ppm (equivalent to a degassing degree of 20%). Next, a filtration treatment was performed. This filtration process is performed by NMS01 manufactured by Pall Corporation.
-L 1 G16H ”, a filter material having a filtration area of 510 cm 2 and a mesh size of 3 μm (Example 1) and a mesh size of 30 μm (Example 2) was loaded with a liquid flow rate of 1 liter / min. I went in. The filter medium was previously immersed in an aqueous PVA solution to remove the internal air. The number of bubbles remaining in the PVA aqueous solution subjected to each of the above treatments was measured by an ultrasonic bubble detector. As a result of the measurement, air bubbles having a diameter of 30 μm or more and air bubbles having a diameter of 30 μm or less are classified, and the remaining numbers of the air bubbles are shown in Table 1.

【0014】比較のために、実施例1と同一のPVA水
溶液を用いて、脱気処理及び濾過処理ともに行わない場
合(比較例1)、脱気処理及び濾過処理ともに行わず、
直径30cmの容器中に20リットル入れ、30分間放
置した場合(比較例2)について、残存気泡数を計測し
た。計測結果を同じく表1に示す。
For comparison, when the same PVA aqueous solution as in Example 1 was used and neither the deaeration nor the filtration was performed (Comparative Example 1), neither the deaeration nor the filtration was performed.
When 20 liters were placed in a container having a diameter of 30 cm and left for 30 minutes (Comparative Example 2), the number of remaining bubbles was counted. Table 1 also shows the measurement results.

【0015】[0015]

【表1】 [Table 1]

【0016】表1より、実施例の残存気泡数は比較例の
残存気泡数に比べて格段に少なく、本発明による脱気処
理後に濾過処理を行う脱泡方法の有効性が確認された。
また、実施例では何れも30μm以上の直径の気泡が完
全に除去され、かつ3μmメッシュの濾材を用いた実施
例2では直径30μm以下の気泡まで完全に除去されて
いることから、濾材の目開きと除去される気泡の直径と
の相関が確認された。
From Table 1, the number of residual bubbles in the examples is much smaller than the number of residual bubbles in the comparative example, confirming the effectiveness of the defoaming method of performing the filtration treatment after the deaeration treatment according to the present invention.
Further, in all of the examples, bubbles having a diameter of 30 μm or more were completely removed, and in Example 2 using a 3 μm mesh filter medium, bubbles having a diameter of 30 μm or less were completely removed. And the diameter of the bubble to be removed was confirmed.

【0017】(実施例3〜実施例5)また、脱気度の影
響を調べるために、実施例1(30μmメッシュの濾材
使用)について、脱気度が96%、90%及び70%と
なるように真空度及び処理時間を調整して脱気処理した
ところ、脱気度が高くなるほど気泡数が減る傾向にある
ことが認められた(表2参照)。
(Examples 3 to 5) In order to investigate the influence of the degree of deaeration, the degree of deaeration is 96%, 90% and 70% in Example 1 (using a 30 μm mesh filter medium). When the degree of vacuum and the processing time were adjusted as described above, the deaeration treatment was performed. As a result, it was recognized that the higher the degree of deaeration, the lower the number of bubbles was (see Table 2).

【0018】[0018]

【表2】 [Table 2]

【0019】更に、粘度150cpのPVA水溶液につ
いて実施例1及び2の処理を行ったところ、上記と同様
の結果が得られた。
Further, when the treatments of Examples 1 and 2 were performed on a PVA aqueous solution having a viscosity of 150 cp, the same results as described above were obtained.

【0020】以上、本発明の脱泡方法に関して主に塗工
液を例にして説明したが、勿論本発明の脱泡方法はその
他の気泡を含有するような液体、しかも低粘度液体から
高粘度液体に至るまで種々の含泡液体に適用可能であ
る。
As described above, the defoaming method of the present invention has been mainly described by taking a coating liquid as an example. Of course, the defoaming method of the present invention can be applied to other liquids containing bubbles, such as low-viscosity liquids to high-viscosity liquids. It is applicable to various foam-containing liquids up to the liquid.

【0021】[0021]

【発明の効果】以上説明したように、本発明の脱泡方法
によれば、含泡液体の粘度に係わらず、短時間で効率よ
く、液中の微小な気泡まで完全に除去することができ
る。しかも、処理に際して設置箇所の制限を受けること
もなく、安価に、含泡液体の脱泡を行うことができる。
As described above, according to the defoaming method of the present invention, fine bubbles in the liquid can be completely removed efficiently in a short time regardless of the viscosity of the liquid. . In addition, the defoaming of the foam-containing liquid can be performed at low cost without being restricted by the installation location during the treatment.

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

【図1】本発明の脱泡方法を実施するための装置構成を
示す模式図である。
FIG. 1 is a schematic view showing an apparatus configuration for performing a defoaming method of the present invention.

【符号の説明】[Explanation of symbols]

1 液調合タンク 3 含泡液体 4 気泡 5 脱泡装置 6 脱気装置 7 濾過装置 DESCRIPTION OF SYMBOLS 1 Liquid preparation tank 3 Bubble-containing liquid 4 Bubbles 5 Defoaming device 6 Deaerator 7 Filtering device

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 気泡を含有する含泡液体から液中の気泡
を取り除く脱泡方法において、前記含泡液体を脱気処理
した後、気泡を捕獲することを特徴とする脱泡方法。
1. A defoaming method for removing bubbles in a liquid from a bubble-containing liquid containing bubbles, the method comprising degassing the bubble-containing liquid and then capturing the bubbles.
【請求項2】 気泡を捕獲する手段として、脱泡目的と
する気泡の直径以下の目開きの濾材を使用して濾過する
ことを特徴とする請求項1に記載の脱泡方法。
2. The defoaming method according to claim 1, wherein the air bubbles are trapped by using a filter medium having an aperture smaller than the diameter of the air bubbles to be defoamed.
【請求項3】 含泡液体中の溶存空気量が、該含泡液体
の飽和溶存空気量の90%以下となるように脱気処理す
ることを特徴とする請求項1または2に記載の脱泡方
法。
3. The degassing process according to claim 1, wherein the deaeration treatment is performed so that the amount of dissolved air in the bubble-containing liquid is 90% or less of the saturated dissolved air amount of the bubble-containing liquid. Foam method.
JP20661197A 1997-07-31 1997-07-31 Defoaming method Expired - Fee Related JP3729374B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20661197A JP3729374B2 (en) 1997-07-31 1997-07-31 Defoaming method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20661197A JP3729374B2 (en) 1997-07-31 1997-07-31 Defoaming method

Publications (2)

Publication Number Publication Date
JPH1147508A true JPH1147508A (en) 1999-02-23
JP3729374B2 JP3729374B2 (en) 2005-12-21

Family

ID=16526254

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20661197A Expired - Fee Related JP3729374B2 (en) 1997-07-31 1997-07-31 Defoaming method

Country Status (1)

Country Link
JP (1) JP3729374B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100812146B1 (en) * 2001-10-31 2008-03-12 주식회사 포스코 Bubble removal apparatus of organic solvent tank
US9440938B2 (en) 2005-09-27 2016-09-13 Shionogi & Co., Ltd. Sulfonamide derivative having PGD2 receptor antagonistic activity

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100812146B1 (en) * 2001-10-31 2008-03-12 주식회사 포스코 Bubble removal apparatus of organic solvent tank
US9440938B2 (en) 2005-09-27 2016-09-13 Shionogi & Co., Ltd. Sulfonamide derivative having PGD2 receptor antagonistic activity

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