JPS58202005A - Apparatus for defoaming high viscosity concentrated liquid - Google Patents
Apparatus for defoaming high viscosity concentrated liquidInfo
- Publication number
- JPS58202005A JPS58202005A JP57085349A JP8534982A JPS58202005A JP S58202005 A JPS58202005 A JP S58202005A JP 57085349 A JP57085349 A JP 57085349A JP 8534982 A JP8534982 A JP 8534982A JP S58202005 A JPS58202005 A JP S58202005A
- Authority
- JP
- Japan
- Prior art keywords
- high viscosity
- slits
- defoaming device
- net
- viscosity concentrated
- 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
- B01D19/0042—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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0036—Flash degasification
-
- 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
- B01D19/0047—Atomizing, spraying, trickling
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】
この発明は一般的には高粘度濃縮液の脱泡装置に関し、
詳しくは高粘度のCOM (微粉状の石炭と重油の混合
物)やカラー液等から、混入している気泡や水滴を高率
に除去することのできる高粘度濃縮液の脱泡装置を提供
せんとするものである。DETAILED DESCRIPTION OF THE INVENTION The present invention generally relates to a defoaming device for high viscosity concentrate;
Specifically, we would like to provide a defoaming device for high-viscosity concentrated liquids that can remove air bubbles and water droplets from high-viscosity COM (a mixture of fine coal and heavy oil) and color liquids at a high rate. It is something to do.
COMやカラー液等の高粘度、高濃度の液体は、最小0
.8mm程度の微小な気泡を大量に包含し、その粘度の
高さ故に脱泡、脱気が思うにまかせない。これをそのま
ま放置しておくと、多量の気泡を含んだCOMやカラー
液を購入或いは使用せざるを得なくなり、不経済であっ
たり使用に不都合を来たす場合が多かった。For high viscosity and high concentration liquids such as COM and color liquids, the minimum
.. It contains a large amount of minute air bubbles of about 8 mm, and its high viscosity makes defoaming and deaeration difficult. If this condition is left as it is, it becomes necessary to purchase or use COM or color liquid containing a large amount of air bubbles, which is often uneconomical or inconvenient to use.
従来このような場合、濃縮液中に含まれる気泡を脱泡す
るために使用される気液分離装置としては、遠心分離機
や衝撃式分離機が使用されている。しかしながらこれら
の装置は設備が天壁になり、しかも気泡の除去効率も約
60%に過ぎない。Conventionally, in such cases, a centrifugal separator or an impact separator has been used as a gas-liquid separator for defoaming air bubbles contained in the concentrated liquid. However, these devices require only a ceiling, and their bubble removal efficiency is only about 60%.
そこで本発明者等は篩を用いた高粘度濃縮液の脱泡装置
について鋭意研究の結果、篩の形状や構造を工夫するこ
とにより、非常に効率良く気泡を除去できるという知見
を得た。As a result of intensive research into a defoaming device for high viscosity concentrated liquids using a sieve, the present inventors have found that air bubbles can be removed very efficiently by devising the shape and structure of the sieve.
すなわち本発明に係る高粘度濃縮液の脱泡装置は、液入
口、液出口を対設し、底部にドレン口を、上部にエアベ
ントをそれぞれ付設した本体を設け、この本体に網状エ
レメントを内蔵させるとともに、網状エレメントを、一
定間隔のスリットを有してほぼ平行に配設され、液入口
側の面が平滑で、かつ隣接した対向側部間に内方に拡が
るテーパー面を形成した多数のバーで構成し、網状エレ
メントに外接して相対的に摺動するスフレバーを設けた
ことを特徴とするも以下図面に基き本発明の実施例につ
いて説明する。第1図において、/は網状エレメントで
。That is, the defoaming device for high viscosity concentrated liquid according to the present invention is provided with a main body having a liquid inlet and a liquid outlet facing each other, a drain port at the bottom and an air vent at the top, and a reticular element built into the main body. In addition, the net-like element is made up of a large number of bars that have slits at regular intervals, are arranged substantially parallel, have a smooth surface on the liquid inlet side, and have a tapered surface that spreads inward between adjacent opposing sides. Embodiments of the present invention will be described below with reference to the drawings. In Figure 1, / is a reticular element.
筒状の網状エレメント/を構成するバー−は、隣接した
バーどうしで限定された開口(スリット)を有し、外周
面、2aが平滑で、隣接した対向側部間に内方に拡がる
テーパー面一すを形成されている。この網状エレメント
/は、開口を有するドラム外周に所定ピッチでワイヤー
をスパイラルに巻装し、このワイヤー表面を切断研磨し
て内方に拡がりを有するよう形成する方法、また貫通す
るVカット溝を所定間隔に穿設し。The bars constituting the cylindrical mesh element have openings (slits) defined by adjacent bars, and have a smooth outer circumferential surface (2a) and a tapered surface that spreads inward between adjacent opposing sides. One is formed. This net-like element/ is produced by winding wire spirally around the outer periphery of a drum having openings at a predetermined pitch, and cutting and polishing the wire surface to form an inward expansion. Perforate at intervals.
このVカット溝を不連続に形成して枠部を一体的に形成
した自己保持能を有するスリット板を、該溝が内方に拡
がりを有するよう円筒形に成形する方法、等により形成
することができる。A slit plate having a self-holding ability in which the V-cut grooves are formed discontinuously and the frame portion is integrally formed is formed by a method of forming the plate into a cylindrical shape so that the groove expands inwardly. I can do it.
上記網状エレメント/の作用表面(バーの外周面)、2
aは平滑で、かつ表面メツシュとなり、この表面に近接
して設置したスフレバー乙を相対的に回転し、スフレバ
ー乙がメツシュに詰った気泡や水泡を掻き取って外周面
2aを再生することができる。Working surface of the mesh element/(outer peripheral surface of the bar), 2
A is smooth and forms a surface mesh, and by rotating the souffle bar B installed close to this surface relatively, the souffle bar O can scrape off air bubbles and water bubbles stuck in the mesh and regenerate the outer peripheral surface 2a. .
網状エレメント/を上述のような平滑面を有するように
構成するには、特に上記Vカット方式で得たものを用い
ることが望ましく、真円度及び平滑度とも、簡単にミク
ロン単位の精度を出すことができる。In order to configure the net-like element/to have a smooth surface as described above, it is particularly desirable to use one obtained by the above-mentioned V-cut method, and both roundness and smoothness can easily achieve micron precision. be able to.
次に第2図乃至第6図は脱泡機構の詳細を示すものであ
る。第2図及び第3図において高粘度濃縮液中に含まれ
る気泡30は1周囲の比重が非常に大きいため、高度に
圧縮されている。Next, FIGS. 2 to 6 show details of the defoaming mechanism. In FIGS. 2 and 3, the air bubbles 30 contained in the high viscosity concentrate have a very large specific gravity around one periphery and are therefore highly compressed.
したがってその表面張力が大きく、真円形状を保持しよ
うとする働きが強く作用しており、液流中においては1
通常破線Aで示したような変形を受けるようなことはな
い。それ故バーdの開口部分に送られてきた気泡30は
この開口部分に滞留し、バー−の外周面2aが平滑であ
ればスフレバー乙のナイフ状の先端7が、滞留する気泡
30を根こそぎ掻き取り、掻き集める。Therefore, its surface tension is large, and it acts strongly to maintain its perfect circular shape.
Normally, the deformation shown by the broken line A does not occur. Therefore, the air bubbles 30 sent to the opening of the bar d stay in this opening, and if the outer circumferential surface 2a of the bar is smooth, the knife-shaped tip 7 of the soufflé bar B will scrape out the remaining air bubbles 30. Take it and scrape it up.
掻き集められて結合し、その径を拡大した気泡30は浮
力を増して液の上面に浮上し、エアベントから排出され
る。The bubbles 30 that have been scraped together, combined, and expanded in diameter increase their buoyancy, float to the top of the liquid, and are discharged from the air vent.
他方、バー−の外周面4aが平滑でないとすれば、第4
図及び第5図に示すように気泡30は、バーdの外周面
a2aよりも奥まった位置で開口部分に係止する。した
がってスフレバー乙は、気泡30を切断しながら掻き取
るので気泡30の除去作用が不充分となり、また作用表
面に目詰まりが生じることとなる。On the other hand, if the outer peripheral surface 4a of the bar is not smooth, the fourth
As shown in the drawings and FIG. 5, the bubble 30 is locked in the opening at a position deeper than the outer peripheral surface a2a of the bar d. Therefore, since the souffle bar O scrapes off the air bubbles 30 while cutting them, the action of removing the air bubbles 30 becomes insufficient, and the working surface becomes clogged.
しかも第6図に示すように、網状エレメントlのバーコ
の外周面、2aが平滑でない場合、スフレバー6の動き
に引きずられるように、気泡30も凹んだバーλ上を回
転して、スフレバー乙の下に圧縮された状態で潜り込み
、遂にはスリットを通過することとなって脱泡効果が大
幅に低下する9
このような網状エレメント/を用いた高粘度濃縮液の脱
泡装置を、第7図乃至第9図に示す。Moreover, as shown in FIG. 6, if the outer circumferential surface 2a of the barco of the net-like element l is not smooth, the air bubbles 30 will also rotate on the concave bar λ, as if dragged by the movement of the souffle bar B, and the soufflé bar O. Figure 7 shows a defoaming device for high viscosity concentrated liquids using such a mesh element. 9 to 9.
第7図及び第8図において、/は上述したような円筒状
の網状エレメントで、一定間隔をもつてほぼ平行に配設
された多数のバー−で構成され、上開口部には蓋3を冠
着し、下部はドレンロダに連通している。IOは側面に
液入口//及び液出口/、、2を対設した本体で、上開
口部には蓋体/3を冠着し、該蓋体/3の上部にスフレ
バー乙を低速回転させる駆動装置Mが載設される。また
/lltは蓋体/3に付設したエアベント、/jは排水
口である。In FIGS. 7 and 8, / is a cylindrical net-like element as described above, consisting of a large number of bars arranged approximately parallel to each other at regular intervals, and a lid 3 is attached to the upper opening. The lower part is connected to the drain rod. IO is a main body with a liquid inlet// and a liquid outlet/, 2 facing each other on the side, a lid body /3 is attached to the upper opening, and a souffle bar O is rotated at low speed on the top of the lid body /3. A drive device M is mounted. Also, /llt is an air vent attached to the lid body /3, and /j is a drain port.
第9図は他の実施例を示すもので、本体−θ内に傾斜し
て設置された網状エレメント、23の上面側に送液する
よう、液入口、2/及び液出口、、2.2を本体、20
側面に配設している。この実施例においても、網状エレ
メント、23を構成するバーの外面は平滑で、隣接した
対向側部間に内方に拡がるテーパー面を形成されている
。FIG. 9 shows another embodiment, in which the liquid inlet, 2/2, and the liquid outlet are installed so as to send liquid to the upper surface side of the net-like element 23, which is installed obliquely in the main body -θ. The main body, 20
It is placed on the side. In this embodiment as well, the outer surfaces of the bars constituting the net-like element 23 are smooth, with tapered surfaces extending inwardly between adjacent opposing sides.
このような構成からなる高粘度濃縮液の脱泡装置におい
て、液入口//から送液されたCOMやカラー液等は、
本体10の周面から網状エレメント/に送液され、気泡
や水泡を除去された液体は、網状エレメント/の液吐出
側から、液出口/、2を紅白して次工程に送液される。In a defoaming device for high viscosity concentrated liquid having such a configuration, COM, color liquid, etc. sent from the liquid inlet //
The liquid is sent from the circumferential surface of the main body 10 to the net-like element/, from which air bubbles and water bubbles have been removed, and is sent to the next process from the liquid discharge side of the net-like element/, with the liquid outlet/2 turned red and white.
この脱泡作業中はスフレバー乙を網状エレメント/に対
して相対的に回動し、常時外周面2aの再生作業を行う
とともに、同時に掻き取った夾雑物や浮遊物をドレンダ
から強制的に排出する。During this defoaming work, the souffle bar B is rotated relative to the net-like element / to constantly regenerate the outer peripheral surface 2a, and at the same time, the scraped foreign matter and floating matter are forcibly discharged from the drainer. .
本発明の高粘度濃縮液の脱泡装置は以上のように構成し
たので、気泡の除去効率が約95%以上と従来例に比し
て飛躍的に向上した。また気泡とともに水滴をも同時に
分離することができ、これを気泡とは別に効率良く回収
することができた。更に除去すべき気泡を網状エレメン
ト/のバーコの間隔を変えることにより、所望の大きさ
に調節することができる。Since the defoaming device for high viscosity concentrated liquid of the present invention is configured as described above, the bubble removal efficiency is about 95% or more, which is dramatically improved compared to the conventional example. In addition, water droplets could be separated from air bubbles at the same time, and these could be efficiently collected separately from air bubbles. Furthermore, the size of the air bubbles to be removed can be adjusted to a desired size by changing the spacing between the bars of the mesh element.
第1図は本発明で使用する網状エレメントの斜視図、第
2図は当該網状エレメントの要部断面斜視図、第3図は
その平面図、第4図は他の網状エレメントの要部断面斜
視図、第5図はその平面図、第6図は気泡の別の挙動を
示す網状エレメントの要部断面斜視図、第7図は本発明
の高粘度濃縮液の脱泡装置の一実施例を示す立面図、第
8図はその平面図、第9図は他の実施例を示す立面図で
ある3
/ 網状エレメント d バー
3 蓋 ダ ドレンロ
乙 スフレバー 7 ナイフ状先端10 本体
// 液入口
/、2 液出口 /3 蓋体
/ダ エアベント /、5 排水口M モーター
IflIl 図
莞4図
i#i5 図
!Pl 2 囚
蔦3図
第 6 図Fig. 1 is a perspective view of a mesh element used in the present invention, Fig. 2 is a cross-sectional perspective view of the main part of the mesh element, Fig. 3 is a plan view thereof, and Fig. 4 is a cross-sectional perspective view of the main part of another mesh element. 5 is a plan view thereof, FIG. 6 is a cross-sectional perspective view of the main part of the mesh element showing another behavior of bubbles, and FIG. 7 is an embodiment of the defoaming device for high viscosity concentrated liquid of the present invention. Fig. 8 is a plan view thereof, and Fig. 9 is an elevational view showing another embodiment.
//Liquid inlet/, 2 Liquid outlet /3 Lid/Da Air vent /, 5 Drain port M Motor IflIl Figure Guan 4 Figure i#i5 Figure! Pl 2 Prisoner Ivy Figure 3 Figure 6
Claims (1)
にエアベントをそれぞれ付設した本体を設け、この本体
に網状エレメントを内蔵させるとともに、網状エレメン
トを、一定間隔のスリットを有してほぼ平行に配設され
、故人口側の面が平滑で、かつ隣接した対向側部間に内
方に拡がるテーパー面を形成した多数のバーで構成し、
網状エレメントに外接して相対的に摺動するスフレバー
を設けたことを特徴とする高粘度濃縮液の脱泡1置。 2、網状エレメントが、貫通するVカット溝を所定間隔
で不連続に穿設して多数のスリットとなし、枠部を一体
的に形成した自己保持能を有するスリット板からなる特
許請求の範囲第1項記載の高粘度濃縮液の脱泡装置。 3、網状エレメントが、スリットが内方に拡“がすを有
するよう円筒形に成形してなる特許請求の範囲第1項ま
たは第2項記載の高粘度濃縮液の脱泡装置。 4、網状エレメントが、傾斜する平板である特許請求の
範囲第1項または第2項記載の高粘度濃縮液の脱泡装置
。[Claims] 1. A main body is provided with a liquid inlet and a liquid outlet facing each other, a drain port at the bottom and an air vent at the top, and a mesh element is built into the main body. Consisting of a large number of bars arranged substantially parallel to each other with slits at intervals, having a smooth surface on the side facing the deceased, and forming a tapered surface that spreads inward between adjacent opposing sides,
A defoaming device for high viscosity concentrated liquids, characterized in that a souffle bar is provided that circumscribes the net-like element and slides relative to it. 2. The net-like element consists of a slit plate having a self-holding ability and having a frame portion integrally formed with a large number of slits formed by discontinuously perforating V-cut grooves at predetermined intervals. The defoaming device for high viscosity concentrated liquid according to item 1. 3. The defoaming device for high viscosity concentrated liquid according to claim 1 or 2, wherein the mesh element is formed into a cylindrical shape so that the slits expand inward. 4. The mesh element 3. A defoaming device for high viscosity concentrated liquid according to claim 1 or 2, wherein the element is an inclined flat plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57085349A JPS58202005A (en) | 1982-05-19 | 1982-05-19 | Apparatus for defoaming high viscosity concentrated liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57085349A JPS58202005A (en) | 1982-05-19 | 1982-05-19 | Apparatus for defoaming high viscosity concentrated liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58202005A true JPS58202005A (en) | 1983-11-25 |
Family
ID=13856195
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57085349A Pending JPS58202005A (en) | 1982-05-19 | 1982-05-19 | Apparatus for defoaming high viscosity concentrated liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58202005A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997010037A1 (en) * | 1995-09-11 | 1997-03-20 | Stücklin & Cie Ag | Water treatment device for degassing and/or de-sludging water in pipes |
JP2006027012A (en) * | 2004-07-14 | 2006-02-02 | Pioneer Electronic Corp | Defoaming method and defoaming apparatus therefor |
WO2014010062A1 (en) * | 2012-07-12 | 2014-01-16 | 株式会社荒井鉄工所 | Degassing method and device for same |
JP2014069099A (en) * | 2012-09-27 | 2014-04-21 | Arai Tekkosho:Kk | Slit nozzle spray defoaming method and device thereof |
CN104324900A (en) * | 2014-09-05 | 2015-02-04 | 无锡贺邦金属制品有限公司 | Silicon foam scraper |
WO2015140904A1 (en) * | 2014-03-17 | 2015-09-24 | 株式会社荒井鉄工所 | Apparatus and method for slit nozzle spray defoaming |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49121269A (en) * | 1973-03-27 | 1974-11-20 |
-
1982
- 1982-05-19 JP JP57085349A patent/JPS58202005A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49121269A (en) * | 1973-03-27 | 1974-11-20 |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997010037A1 (en) * | 1995-09-11 | 1997-03-20 | Stücklin & Cie Ag | Water treatment device for degassing and/or de-sludging water in pipes |
JP2006027012A (en) * | 2004-07-14 | 2006-02-02 | Pioneer Electronic Corp | Defoaming method and defoaming apparatus therefor |
WO2014010062A1 (en) * | 2012-07-12 | 2014-01-16 | 株式会社荒井鉄工所 | Degassing method and device for same |
JPWO2014010062A1 (en) * | 2012-07-12 | 2016-06-20 | 株式会社荒井鉄工所 | Defoaming method and apparatus |
JP2014069099A (en) * | 2012-09-27 | 2014-04-21 | Arai Tekkosho:Kk | Slit nozzle spray defoaming method and device thereof |
WO2015140904A1 (en) * | 2014-03-17 | 2015-09-24 | 株式会社荒井鉄工所 | Apparatus and method for slit nozzle spray defoaming |
CN104324900A (en) * | 2014-09-05 | 2015-02-04 | 无锡贺邦金属制品有限公司 | Silicon foam scraper |
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