JPS6335287B2 - - Google Patents
Info
- Publication number
- JPS6335287B2 JPS6335287B2 JP54152492A JP15249279A JPS6335287B2 JP S6335287 B2 JPS6335287 B2 JP S6335287B2 JP 54152492 A JP54152492 A JP 54152492A JP 15249279 A JP15249279 A JP 15249279A JP S6335287 B2 JPS6335287 B2 JP S6335287B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- stirring shaft
- foam
- saucer
- containing liquid
- 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
Links
- 238000003756 stirring Methods 0.000 claims description 21
- 239000006260 foam Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 8
- 239000003973 paint Substances 0.000 claims description 6
- 239000002002 slurry Substances 0.000 claims description 5
- 239000007788 liquid Substances 0.000 description 29
- 238000011282 treatment Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000002562 thickening agent Substances 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
Description
【発明の詳細な説明】
本発明は水を媒体として、4〜80μ程度の水不
溶性樹脂粒子を固形分濃度で10〜70重量%の範囲
で分散させ、さらに必要に応じて着色剤、界面活
性剤、増粘剤等を含有させてなるスラリー状塗料
中の泡を破壊し脱泡処理するための脱泡処理装置
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention involves dispersing water-insoluble resin particles of approximately 4 to 80 μm in solid content in a solids concentration range of 10 to 70% by weight, using water as a medium, and adding a coloring agent and a surfactant as necessary. The present invention relates to a defoaming treatment device for destroying and defoaming bubbles in a slurry paint containing a thickening agent, a thickener, and the like.
従来、高粘度液体であるスラリー状塗料(以下
単に液体という)はその製造過程において泡を含
むことが多い。そのため粒子が泡の表面に吸着さ
れ泡を媒体として再凝集などの欠陥現象を呈する
ので製品の品質向上の観点から脱泡処理は必須の
工程である。従来の脱泡処理は大きく分類すると
下記三方式に分類される。 Conventionally, slurry paints (hereinafter simply referred to as liquids), which are high viscosity liquids, often contain bubbles during the manufacturing process. Therefore, the particles are adsorbed to the surface of the foam and exhibit defect phenomena such as re-aggregation using the foam as a medium, so defoaming treatment is an essential step from the viewpoint of improving product quality. Conventional defoaming treatments can be broadly classified into the following three methods.
(1) 真空室に含泡液体を投入し撹拌する事によつ
て破泡、脱泡する方式。(1) A method of breaking and defoaming by pouring a foam-containing liquid into a vacuum chamber and stirring it.
(2) 含泡液体に高速渦流を発生させる事により破
泡、脱泡する方式。(2) A method of breaking and defoaming bubbles by generating high-speed vortices in a foam-containing liquid.
(3) 含泡液体を超音波により破泡、脱泡する方
式。(3) A method of breaking and defoaming foam-containing liquids using ultrasonic waves.
しかしながら、これら従来方式には種々の技術
的問題点があり、未だ完全なる技術は確立されて
ない。例えば(1)方式は、高粘度液体の場合には脱
泡にかなりの長時間を要し、連続運転が難しい事
の欠点があつた。また(2)方式では含泡液体中に固
形物が存在していると遠心力によつて沈殿分離を
起す欠点があつた。(3)方式では含泡液体中に固形
物が存在しているとしばしば固形物が凝集する欠
点があつた。 However, these conventional methods have various technical problems, and a perfect technology has not yet been established. For example, method (1) has the disadvantage that it takes a considerable amount of time to defoam in the case of high viscosity liquids, making continuous operation difficult. In addition, method (2) had the disadvantage that if solids were present in the foam-containing liquid, precipitation would occur due to centrifugal force. Method (3) had the disadvantage that solids often agglomerated when they were present in the foam-containing liquid.
本発明は以上の如き従来技術に鑑みて、脱泡ス
ピードが極めて迅速であり、かつ連続運転可能で
あり、含泡液体中に粒径4〜80μ程度の樹脂粒子
が存在していても沈殿分離の生じない脱泡処理装
置を提供するものである。 In view of the above-mentioned conventional technology, the present invention has an extremely rapid defoaming speed, can be operated continuously, and can perform precipitation separation even when resin particles with a particle size of about 4 to 80 μm are present in a foam-containing liquid. The purpose of the present invention is to provide a defoaming treatment device that does not cause air bubbles.
即ち本発明は、減圧手段を備えているタンク;
駆動装置により駆動され、かつタンクの中心部に
設置されている撹拌軸;該撹拌軸の下端に取付け
られた撹拌用円板状デイスク;上記撹拌軸の中央
付近に撹拌軸とともに回転する如く取付けられて
いる受皿;該受皿上にタンク外部から含泡液体を
供給するための手段;及び、タンク底部に設置さ
れた液体取出口;からなる脱泡処理装置に関する
ものである。 That is, the present invention provides a tank equipped with a pressure reducing means;
A stirring shaft driven by a drive device and installed in the center of the tank; A disc-shaped stirring disk attached to the lower end of the stirring shaft; A stirring disk mounted near the center of the stirring shaft so as to rotate with the stirring shaft. The present invention relates to a defoaming treatment device comprising: a receiving tray; a means for supplying a foam-containing liquid onto the receiving tray from outside the tank; and a liquid outlet installed at the bottom of the tank.
以下図面を参考として本発明を具体例につき詳
細に説明する。 Hereinafter, the present invention will be described in detail with reference to specific examples with reference to the drawings.
第1図は本発明による代表的脱泡処理装置の使
用状態縦断面図である。本装置はタンク1を有
し、これには減圧手段、例えば真空ポンプ2が付
設されている。また、タンク内には駆動装置(図
示せず)により駆動され、かつタンクの中心部に
撹拌軸3が設置されており、その下端に撹拌用デ
イスク(円板状のもの)4が付設されている。さ
らに撹拌軸3には、パイプ5より供給される含泡
液体を受け入れるための受皿6が取付けられてい
る。受皿6は撹拌軸3とともに回転し、受皿6に
供給された含泡液体7が回転遠心力によりタンク
側壁に飛散し側壁にそつて静かに流れ落ちるよう
に大きさと形状を定めるのが好ましい。受皿6に
供給された含泡液体7は受皿6の回転により強い
遠心力と慣性力を受けてスピン現象を起こしつつ
気泡が破泡されるので、受皿6の表面を凹凸状に
したりあるいは溝を付けたりするとさらに破泡が
容易となる。 FIG. 1 is a longitudinal sectional view of a typical defoaming treatment apparatus according to the present invention in use. The device has a tank 1, to which pressure reducing means, for example a vacuum pump 2, are attached. Furthermore, inside the tank, there is a stirring shaft 3 that is driven by a drive device (not shown) and is installed in the center of the tank, and a stirring disk (disc-shaped) 4 is attached to the lower end of the stirring shaft 3. There is. Furthermore, a saucer 6 is attached to the stirring shaft 3 for receiving the foam-containing liquid supplied from the pipe 5. It is preferable that the size and shape of the saucer 6 be determined so that the saucer 6 rotates together with the stirring shaft 3, and the foam-containing liquid 7 supplied to the saucer 6 is scattered onto the side wall of the tank by rotational centrifugal force and gently flows down along the sidewall. The bubble-containing liquid 7 supplied to the saucer 6 is subjected to strong centrifugal force and inertial force due to the rotation of the saucer 6, causing a spin phenomenon and causing the bubbles to burst. Therefore, the surface of the saucer 6 may be made uneven or grooved. If it is added, it will be easier to break the bubbles.
本発明の脱泡装置の使用時においては、先ずバ
ルブ8,9,10を閉じバルブ11を開き、真空
ポンプ2を運転し、タンク1内を減圧にする。圧
力については含泡液体の粘度等により適宜決定さ
れるが、スラリー状塗料の場合は−700〜−740mm
Hg程度が適当である。圧力を減圧計12にて確
認し、所定の圧力まで減圧された後、撹拌軸3を
回転させつつバルブ8を開口し、含泡液体を受皿
6の中央部にそそぐ。含泡液体は、受皿6の回転
により微粒子化され破泡されつつタンク側壁に飛
散する。側壁に付着した後においても含まれてい
るわずかな気泡はタンク下部において撹拌用デイ
スク4により起された渦流により大きく成長し、
速やかに脱泡される。タンク1の下部に落ちてく
る液体の液面が順次上昇し、受皿6の下面に達す
るとバルブ8を閉じて含泡液体の供給をストツプ
する。数分間さらに運転を続け液面に浮上してい
る泡を受皿6の裏面で破泡した後、駆動を止め、
真空ポンプ2を停止し、バルブ10を開口しタン
ク1内部を常圧に戻す。次にバルブ9を開口し、
取出口13よりポンプ14を運転して脱泡処理し
た液体を系外に取出す。 When using the defoaming device of the present invention, first, the valves 8, 9, and 10 are closed, the valve 11 is opened, and the vacuum pump 2 is operated to reduce the pressure inside the tank 1. The pressure is determined appropriately depending on the viscosity of the foam-containing liquid, but in the case of slurry paint it is -700 to -740 mm.
Hg level is appropriate. The pressure is checked with the pressure reducing gauge 12, and after the pressure has been reduced to a predetermined pressure, the valve 8 is opened while the stirring shaft 3 is rotated, and the foam-containing liquid is poured into the center of the saucer 6. The foam-containing liquid is turned into fine particles by the rotation of the saucer 6, and the bubbles are broken and scattered onto the side wall of the tank. Even after adhering to the side wall, the small amount of air bubbles contained in the tank grow larger due to the vortex generated by the stirring disk 4 at the bottom of the tank.
It is defoamed quickly. The liquid level of the liquid falling at the bottom of the tank 1 rises one after another, and when it reaches the bottom surface of the saucer 6, the valve 8 is closed to stop the supply of the bubble-containing liquid. After continuing to operate for several minutes to break the bubbles floating on the liquid surface on the back side of the saucer 6, the drive was stopped.
The vacuum pump 2 is stopped, the valve 10 is opened, and the inside of the tank 1 is returned to normal pressure. Next, open the valve 9,
The pump 14 is operated through the outlet 13 to take out the defoamed liquid from the system.
なお、スラリー状塗料の種類により液面の泡が
完全に破泡しにくい場合は、液体を全て系外に取
出さず、一部液体を残し、次回の運転で液面上の
泡を破泡してもよい。 Depending on the type of slurry paint, if the bubbles on the liquid surface are difficult to completely break, do not remove all of the liquid from the system, leave some of the liquid, and break the bubbles on the liquid surface during the next operation. You may.
第1図は本発明の代表的な脱泡処理装置の使用
状態縦断面図である。
1:タンク、2:真空ポンプ、3:撹拌軸、
4:撹拌用デイスク、5:含泡液体導入供給パイ
プ、6:受皿、7:含泡液体、8,9,10,1
1:バルブ、12:減圧計、13:脱泡処理され
た液体の取出口、14:ポンプ。
FIG. 1 is a longitudinal sectional view of a typical defoaming treatment apparatus of the present invention in use. 1: Tank, 2: Vacuum pump, 3: Stirring shaft,
4: Stirring disk, 5: Foam-containing liquid introduction and supply pipe, 6: Receiver, 7: Foam-containing liquid, 8, 9, 10, 1
1: Valve, 12: Decompression gauge, 13: Defoamed liquid outlet, 14: Pump.
Claims (1)
り駆動され、かつタンクの中心部に設置されてい
る撹拌軸;該拌撹軸の下端に取付けられた撹拌用
円板状デイスク;上記撹拌軸の中央付近に撹拌軸
とともに回転する如く取付けられている受皿;該
受皿上にタンク外部から含泡スラリー状塗料を供
給するための手段;及び、タンク底部に配置され
た塗料取出口;からなる脱泡処理装置。1 A tank equipped with a pressure reduction means; A stirring shaft driven by a drive device and installed in the center of the tank; A disc-shaped stirring disc attached to the lower end of the stirring shaft; The center of the stirring shaft A defoaming process consisting of a saucer mounted nearby so as to rotate with the stirring shaft; a means for supplying foam-containing slurry paint onto the saucer from outside the tank; and a paint outlet located at the bottom of the tank. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15249279A JPS5676214A (en) | 1979-11-27 | 1979-11-27 | Defoaming processor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15249279A JPS5676214A (en) | 1979-11-27 | 1979-11-27 | Defoaming processor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5676214A JPS5676214A (en) | 1981-06-23 |
JPS6335287B2 true JPS6335287B2 (en) | 1988-07-14 |
Family
ID=15541643
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15249279A Granted JPS5676214A (en) | 1979-11-27 | 1979-11-27 | Defoaming processor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5676214A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0576702A (en) * | 1991-09-24 | 1993-03-30 | Ngk Insulators Ltd | Supply defoaming method and vacuum defoaming equipment using same |
US7588631B2 (en) * | 2006-02-15 | 2009-09-15 | The Western States Machine Company | Vacuum deaerator |
CN102304808A (en) * | 2011-09-01 | 2012-01-04 | 吴江市隆泰喷织厂 | Water absorption device for water-jet loom |
JP6302321B2 (en) * | 2014-03-28 | 2018-03-28 | プライミクス株式会社 | Liquid treatment equipment for battery electrode coating production |
CN109663388B (en) * | 2018-12-18 | 2021-04-02 | 合肥信达膜科技有限公司 | A deaeration device for preparing milipore filter |
CN110578723B (en) * | 2019-10-24 | 2021-12-14 | 江苏塑光汽车部件有限公司 | Hydraulic oil tank |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5051970A (en) * | 1972-12-04 | 1975-05-09 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5255155Y2 (en) * | 1973-08-27 | 1977-12-13 |
-
1979
- 1979-11-27 JP JP15249279A patent/JPS5676214A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5051970A (en) * | 1972-12-04 | 1975-05-09 |
Also Published As
Publication number | Publication date |
---|---|
JPS5676214A (en) | 1981-06-23 |
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