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JPH05103905A - Bubble separation equipment - Google Patents

Bubble separation equipment

Info

Publication number
JPH05103905A
JPH05103905A JP3269328A JP26932891A JPH05103905A JP H05103905 A JPH05103905 A JP H05103905A JP 3269328 A JP3269328 A JP 3269328A JP 26932891 A JP26932891 A JP 26932891A JP H05103905 A JPH05103905 A JP H05103905A
Authority
JP
Japan
Prior art keywords
separated
liquid
separation tank
bubble
liquid level
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
JP3269328A
Other languages
Japanese (ja)
Other versions
JP2977341B2 (en
Inventor
Yoshitomo Sakai
能具 酒井
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.)
RYOWA KAIYO KAIHATSU KK
Mitsubishi Heavy Industries Ltd
Original Assignee
RYOWA KAIYO KAIHATSU KK
Mitsubishi Heavy Industries 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 RYOWA KAIYO KAIHATSU KK, Mitsubishi Heavy Industries Ltd filed Critical RYOWA KAIYO KAIHATSU KK
Priority to JP3269328A priority Critical patent/JP2977341B2/en
Publication of JPH05103905A publication Critical patent/JPH05103905A/en
Application granted granted Critical
Publication of JP2977341B2 publication Critical patent/JP2977341B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To provide an equipment for efficiently removing material to be separated to form treated liquid irrespective of the change in concentration of the material to be separated in feed liquid. CONSTITUTION:When foams formed by making material to be separated in feed liquid stick to bubbles generated by a bubble generator 2 is accumulated over the liquid surface 8 of a separation tack 1, liquid level adjusting means 6, 13, 14, 15 are operated by a control signal from a controller 16 to raise the liquid surface 8 of the separation tank 1, causing the removal of the foams to which the material to be separated sticks to be facilitated by a defoaming device 3. Thereby bubble separation equipment which has high concentration efficiency of material to be separated and forms treated liquid from which material to be separated is properly removed irrespective of the charge in concentration of material to be separated is obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、魚の蓄養槽等の水処理
装置を含む排水処理装置、油水分離装置および微粉精鉱
分離装置等の気泡分離装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bubble separation device such as a waste water treatment device including a water treatment device such as a fish farm, an oil / water separation device and a fine powder concentrate separation device.

【0002】[0002]

【従来の技術】従来の気泡分離装置は、図6に示すよう
に側部に原液流入部04が設けられた分離槽01、同分
離槽01内下部に設けられた気泡発生装置02、上記分
離槽01の上部に設けられ回転羽根010とモータ01
1を有する泡除去装置03、上記分離槽01の外側に設
けられ内部が連通した処理液流出部05、同処理液流出
部05の側壁05a上端に設けられ手作業により昇降可
能な可動堰06、および上記処理液流出部05の外側に
設けられた処理液流出口012を備えていた。
2. Description of the Related Art As shown in FIG. 6, a conventional air bubble separation device includes a separation tank 01 having a stock solution inflow portion 04 on its side, a bubble generation device 02 provided in the lower portion of the separation tank 01, and the above separation. Rotating blade 010 and motor 01 provided on the upper part of tank 01
A bubble removing device 03 having the above-mentioned 1, a processing liquid outflow portion 05 provided outside the separation tank 01 and communicating with the inside, a movable weir 06 provided at an upper end of a side wall 05a of the processing liquid outflow portion 05 and capable of being manually moved up and down, And a treatment liquid outlet 012 provided outside the treatment liquid outflow portion 05.

【0003】上記において、原液流入部04より原液と
ともに供給された分離槽01中の被分離物は、気泡発生
装置02により槽01中に発生した気泡7に付着し、こ
の気泡7は浮上し、液面8上に泡9を生じていた。
In the above description, the substance to be separated in the separation tank 01 supplied together with the stock solution from the stock solution inflow portion 04 adheres to the bubbles 7 generated in the tank 01 by the bubble generating device 02, and the bubbles 7 float up. Bubbles 9 were formed on the liquid surface 8.

【0004】上記液面8上に生じた泡9は次々に発生す
る泡9により、上方に押上げられるが、上方に移動する
際に泡9の中に含まれる液分が減少し、被分離物がより
濃縮される。
The bubbles 9 generated on the liquid surface 8 are pushed up by the bubbles 9 generated one after another, but when moving upward, the liquid content contained in the bubbles 9 is reduced, and the bubbles 9 are separated. The thing is more concentrated.

【0005】上記液面8上に押上げられた泡9は、モー
タ011により回転する回転羽根010によりすくい出
されるため、泡9とともに被分離物が除去されていた。
また、上記により被分離物が除去された処理液は、処理
液流出部05を経て処理液流出口012より流出してい
た。
The bubbles 9 pushed up on the liquid surface 8 are scooped out by the rotary blades 010 rotated by the motor 011. Therefore, the substances to be separated are removed together with the bubbles 9.
Further, the treatment liquid from which the substances to be separated have been removed as described above has flowed out of the treatment liquid outlet 012 through the treatment liquid outflow portion 05.

【0006】[0006]

【発明が解決しようとする課題】従来の装置において
は、下記の課題があった。 (1)被分離物の濃度が低い場合、泡の発生量が少なく
その結果、泡の高さが低くなり泡除去装置に届かないた
め、被分離物が除去不能となる。 (2)被分離物の濃度が濃すぎる場合、泡の発生量が多
く、除去は易しくなるが、泡に含まれる液分の量が多い
状態で泡が除去されるため、液分が大幅に減少し、被分
離物の濃縮効率が低い。
The conventional apparatus has the following problems. (1) When the concentration of the substance to be separated is low, the amount of foam generated is small, and as a result, the height of the bubble is low and it does not reach the bubble removing device, so that the substance to be separated cannot be removed. (2) When the concentration of the substance to be separated is too high, the amount of bubbles generated is large and removal is easy, but since the bubbles are removed in a state where the amount of liquid contained in the bubbles is large, the amount of liquid is significantly increased. And the efficiency of concentrating the substance to be separated is low.

【0007】本発明は上記の課題を解決しようとするも
のである。
The present invention is intended to solve the above problems.

【0008】[0008]

【課題を解決するための手段】本発明の気泡分離装置
は、気泡発生装置と泡除去装置と原液流入部が設けられ
た分離槽、同分離槽と内部が連通した処理液流出部、お
よび同流出部に隣接して設けられた処理液流出口を備え
た気泡分離装置において、上記処理液流出部に設けられ
た液面調整手段、および同液面調整手段に接続された制
御装置を備えたことを特徴としている。
A bubble separating device of the present invention comprises a bubble generating device, a bubble removing device, a separation tank provided with a stock solution inflow section, a processing solution outflow section communicating with the separation tank and an inside thereof. A bubble separation device having a processing liquid outlet provided adjacent to an outflow portion, comprising a liquid level adjusting means provided in the processing liquid outflow portion, and a control device connected to the liquid level adjusting means. It is characterized by

【0009】[0009]

【作用】上記において、通常は分離槽及び処理液流出部
の液面を一定のレベルに下げ、原液流入部より原液を供
給し、処理液流出口より処理液を排出させ、本発明の装
置を運転する。
In the above, normally, the liquid level in the separation tank and the processing solution outflow portion is lowered to a certain level, the undiluted solution is supplied from the undiluted solution inflow portion, and the undissolved solution is discharged from the undissolved solution outlet port. drive.

【0010】上記分離槽中においては、気泡発生装置に
より発生する気泡が原液中に含まれる被分離物を付着し
て上昇し、被分離物濃度に応じた量の泡を液面上に生成
した後、上部の泡の一部はもとの液状にもどり、泡中の
被分離物の濃度を上昇させる。
In the above separation tank, the bubbles generated by the bubble generator adhere to the substance to be separated contained in the undiluted solution and rise to generate bubbles in an amount corresponding to the concentration of the substance to be separated on the liquid surface. After that, a part of the bubbles in the upper part returns to the original liquid state, and the concentration of the substance to be separated in the bubbles is increased.

【0011】本発明の装置においては、制御装置と液面
調整手段によって分離槽及び処理液流出部の液面の調整
が可能なため、上記泡中の被分離物の濃度が適量になる
か又は一定時間経過後、制御装置からの制御信号により
液面調整手段を作動させて液面を上昇させ、泡の除去に
適したレベルとする。
In the apparatus of the present invention, since the liquid level in the separation tank and the processing liquid outflow portion can be adjusted by the control unit and the liquid level adjusting means, the concentration of the substance to be separated in the foam becomes appropriate. After a certain period of time, the liquid level adjusting means is activated by the control signal from the control device to raise the liquid level to a level suitable for removing bubbles.

【0012】上記液面が上昇状態の間に泡とともに被分
離物を泡除去装置により除去し、その後、再び上記液面
を液面調整手段により通常の状態に戻す。
While the liquid level is in the ascending state, the object to be separated together with bubbles is removed by the bubble removing device, and then the liquid level is returned to the normal state by the liquid level adjusting means.

【0013】本発明の装置においては、上記のように処
理液流出部に液面調整手段を設け、分離槽の液面を容易
に調整できるものとしたため、被分離物の濃度変化に係
わらず、被分離物の濃縮効率が高く、被分離物が適切に
除去された処理液の生成が可能な装置を実現する。
In the apparatus of the present invention, since the liquid level adjusting means is provided in the processing liquid outflow portion as described above so that the liquid level in the separation tank can be easily adjusted, regardless of the change in the concentration of the substance to be separated, (EN) An apparatus capable of producing a treatment liquid in which a substance to be separated is highly concentrated and a substance to be separated is appropriately removed.

【0014】[0014]

【実施例】本発明の第1実施例を図1及び図2に示す。
図1及び図2に示す本実施例は、下部に気泡発生装置2
と上部に泡除去装置3と側部に原液流入部4が設けられ
た分離槽1、同分離槽1の外側に配設され同分離槽1と
内部が連通し側壁5aの上部に流出部可動堰6が設けら
れた処理液流出部5、および同流出部5の外側に設けら
れた処理液流出口12を備えた気泡分離装置において、
上記処理液流出部5の側壁5aの上部に設けられた流出
部可動堰6に結合された駆動装置13、同駆動装置13
に接続された開閉装置14、および同開閉装置14に接
続された駆動源15と制御装置16を備えており、上記
流出部可動堰6と駆動装置13と開閉装置14と駆動源
15により液面調整手段が形成されている。なお、本実
施例は処理液流出部5の関連装置以外は従来の装置と同
様のため、その詳細説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention is shown in FIGS.
In this embodiment shown in FIGS. 1 and 2, the bubble generating device 2 is provided at the bottom.
And a separation tank 1 provided with a bubble removing device 3 on the upper side and a stock solution inflow section 4 on the side, and the separation section 1 is arranged outside the separation tank 1 and communicates with the inside of the separation tank 1, and the outflow portion can be moved to the upper part of the side wall 5a In a bubble separation device including a processing liquid outflow portion 5 provided with a weir 6, and a processing liquid outlet 12 provided outside the outflow portion 5,
The drive device 13 and the drive device 13 coupled to the outflow-portion movable weir 6 provided on the side wall 5a of the processing liquid outflow portion 5.
And a drive device 15 and a control device 16 connected to the opening / closing device 14, and the movable weir 6, the drive device 13, the opening / closing device 14, and the driving source 15 connected to the outflow part. Adjustment means are formed. Since the present embodiment is the same as the conventional apparatus except for the related apparatus of the processing liquid outflow unit 5, detailed description thereof will be omitted.

【0015】上記において、駆動源15より供給された
油圧、水圧又、空気圧又は電気等の駆動力は制御装置1
6からの指令信号により開閉される電磁弁等よりなる開
閉装置14により制御されて駆動装置13に供給され、
同駆動装置13は図2に示すようにガイド17によりガ
イドされた流出部可動堰6を駆動する。
In the above, the driving force such as hydraulic pressure, hydraulic pressure, pneumatic pressure or electricity supplied from the driving source 15 is applied to the control device 1.
6, which is controlled by an opening / closing device 14 formed of a solenoid valve or the like that is opened / closed in response to a command signal from 6, and is supplied to the drive device 13,
The drive device 13 drives the outflow-portion movable weir 6 guided by the guide 17 as shown in FIG.

【0016】上記流出部可動堰6は上記の駆動機構が接
続されているため、この駆動機構により、分離槽1内の
泡の状態に合わせて流出部可動堰6を間歇的に昇降させ
ることができ、この可動堰6の昇降により液面8を調整
することができるため、原液中の被分離物の適切な除去
を可能とする。
Since the above-mentioned drive mechanism is connected to the outflow movable weir 6, the outflow movable weir 6 can be intermittently moved up and down according to the state of bubbles in the separation tank 1 by this drive mechanism. Since the liquid level 8 can be adjusted by raising and lowering the movable weir 6, it is possible to appropriately remove the substance to be separated in the stock solution.

【0017】本実施例においては、上記のように流出部
可動堰の間歇的昇降を可能としたため、被分離物の濃度
の変化に係わらず、被分離物が常に適切に除去された処
理液の生成を可能とした。
In this embodiment, the intermittent movement of the movable weir of the outflow part is possible as described above, so that the treatment liquid in which the substance to be separated is always appropriately removed is removed regardless of the change in the concentration of the substance to be separated. It was possible to generate.

【0018】本発明の第2実施例を図3により説明す
る。図3に示す本実施例は、上記第1実施例における上
下に昇降する流出部可動堰6に替えて、チェーンやベル
ト等よりなる伝達装置20を介してモータ18により回
転する回転堰19により液面調整手段を形成し、同回転
堰19の回転角度により液面8のレベルを調整するもの
であり、また、泡除去装置22としてはベルトスキマを
用い、更に、処理液流出部5の側壁5aには開閉装置2
1が設けられたものである。
A second embodiment of the present invention will be described with reference to FIG. The present embodiment shown in FIG. 3 uses a rotary weir 19 rotated by a motor 18 via a transmission device 20 composed of a chain, a belt or the like, instead of the outflow movable weir 6 that moves up and down in the first embodiment. A surface adjusting means is formed to adjust the level of the liquid surface 8 by the rotation angle of the rotary weir 19, a belt skimmer is used as the bubble removing device 22, and the side wall 5a of the processing liquid outflow portion 5 is used. Switchgear 2
1 is provided.

【0019】本実施例の作用及び効果については第1実
施例のそれとほヾ同様である。なお、上記回転堰19を
回転させるためのモータ18は図示しない制御装置によ
り第1実施例と同様に制御される。
The operation and effect of this embodiment are almost the same as those of the first embodiment. The motor 18 for rotating the rotary weir 19 is controlled in the same manner as in the first embodiment by a controller (not shown).

【0020】なお図3では、開閉装置21を追加してい
るが、この場合は開閉装置21を開とした状態が低位液
面でこれを制御装置により閉とすると、回転堰19に相
当する液面迄、分離槽の液面が上昇し、泡を排出する。
この場合に回転堰19を微調整すればより高精度の排出
コントロールができる。
In FIG. 3, the switchgear 21 is added, but in this case, when the switchgear 21 is open and the control device closes the liquid level, the liquid equivalent to the rotary dam 19 is reached. Up to the surface, the liquid level in the separation tank rises and bubbles are discharged.
In this case, if the rotary weir 19 is finely adjusted, more precise discharge control can be performed.

【0021】本発明の第3実施例を図4により説明す
る。図4に示す本実施例は、第1実施例における分離槽
1に替えて蓋付分離槽23としてものである。同分離槽
23の側壁下部には処理液流出管25が接続され、処理
液流出部5内を上方に向けて配設されており、処理液流
出管25上端にはシール部25aを介して筒状の可動堰
24が設けられ、これらが第1実施例における流出部可
動堰6の役割を果たしている。
A third embodiment of the present invention will be described with reference to FIG. In this embodiment shown in FIG. 4, the separation tank 1 with a lid is replaced with the separation tank 1 in the first embodiment. A processing liquid outflow pipe 25 is connected to the lower part of the side wall of the separation tank 23, and is arranged so that the inside of the processing liquid outflow portion 5 faces upward. Shaped movable weirs 24 are provided, and these play the role of the outflow portion movable weir 6 in the first embodiment.

【0022】また、上記処理液流出部5に接続された処
理液流出口12には処理液濃度モニタ装置26が設けら
れ、同モニタ装置26は制御装置16に接続されてい
る。この制御装置16は駆動源15に接続されており、
駆動源15は上記可動堰24に結合された駆動装置13
に接続されている。なお、本実施例においては、上記可
動堰24と駆動装置13と駆動源15により液面調整手
段が形成されている。
A processing liquid concentration monitor 26 is provided at the processing liquid outlet 12 connected to the processing liquid outlet 5, and the monitoring device 26 is connected to the controller 16. This controller 16 is connected to the drive source 15,
The driving source 15 is a driving device 13 connected to the movable weir 24.
It is connected to the. In the present embodiment, the movable weir 24, the driving device 13, and the driving source 15 form a liquid level adjusting means.

【0023】上記において、可動堰24が昇降して分離
槽23の液面8を調整する点は第1実施例と同様である
が、本実施例の場合には、処理液中の被分離物の濃度が
処理液濃度モニタ装置26により検出され、その検出信
号により可動堰24が昇降される点に特徴がある。
In the above description, the movable weir 24 is moved up and down to adjust the liquid level 8 of the separation tank 23, which is the same as in the first embodiment. However, in the case of this embodiment, the substance to be separated in the treatment liquid is separated. Is characterized in that the concentration of the treatment liquid is detected by the treatment liquid concentration monitor device 26, and the movable weir 24 is moved up and down by the detection signal.

【0024】即ち、処理液濃度モニタ装置26の検出信
号は制御装置16に入力され、制御装置16は制御信号
を駆動源15に入力して駆動装置13を作動させ、処理
液中の被分離物の濃度が設定した値より濃い場合は、分
離不十分として、分離槽23内の液面9が上昇するよう
に可動堰24を上昇させる。また、濃度が薄い場合は可
動堰24を下降され処理能力の向上をはかる。なお、上
記処理液濃度モニタ装置26による液面コントロール
は、排出泡の濃度,重量等のモニタ装置によるコントロ
ールに代えることも可能である。
That is, the detection signal of the treatment liquid concentration monitor device 26 is input to the control device 16, and the control device 16 inputs the control signal to the drive source 15 to operate the drive device 13 to separate the substance to be separated in the treatment liquid. If the concentration is higher than the set value, it is determined that the separation is insufficient, and the movable weir 24 is raised so that the liquid level 9 in the separation tank 23 rises. If the concentration is low, the movable weir 24 is lowered to improve the processing capacity. The liquid level control by the treatment liquid concentration monitor device 26 can be replaced with the control by the monitor device for the concentration, weight and the like of the discharged bubbles.

【0025】本発明の第4実施例を図5により説明す
る。図5に示す本実施例は、第3実施例と同様に蓋付分
離槽23を用い、その側壁下部に処理液流出管35,3
6を接続するものであるが、本実施例において用いる処
理液流出管35は上端に開口部35aを有する他、中間
の側部にも開口部35bが設けられており、上端の開口
部35aには,同開口部35aをパッキンにより開閉す
る駆動装置13が設けられ、中間の開口部35bには、
パッキン28と弁体30と弁棒31を有し逃がし口3
3,34が設けられたシリンダ装置27が設けられたも
のである。このシリンダ装置27は蓋付分離槽23に原
液を供給するポンプ22の吐出口に接続された2本の管
路29が接続され、1本は直接、他の1本は開閉装置2
1を介して接続されており、同開閉装置21と上記駆動
装置13は制御装置16に接続されている。なお、本実
施例においては、上記駆動装置13とシリンダ装置27
と開閉装置21と処理液流出管35,36と管路29に
より液面調整手段が形成されている。
A fourth embodiment of the present invention will be described with reference to FIG. In this embodiment shown in FIG. 5, the separation tank with a lid 23 is used as in the third embodiment, and the processing liquid outflow pipes 35, 3 are provided at the lower portions of the side walls thereof.
6, the processing liquid outflow pipe 35 used in the present embodiment has an opening 35a at the upper end, and an opening 35b is also provided at an intermediate side part, and the opening 35a is provided at the upper end. Is provided with a drive device 13 that opens and closes the opening 35a with packing, and an intermediate opening 35b is
Relief port 3 with packing 28, valve body 30 and valve rod 31
A cylinder device 27 provided with 3, 34 is provided. In this cylinder device 27, two pipe lines 29 connected to the discharge port of the pump 22 for supplying the stock solution to the lidded separation tank 23 are connected, one is directly, and the other one is the opening / closing device 2
1, and the opening / closing device 21 and the drive device 13 are connected to the control device 16. In this embodiment, the drive device 13 and the cylinder device 27 are used.
The opening / closing device 21, the processing liquid outflow pipes 35 and 36, and the pipe 29 form a liquid level adjusting means.

【0026】上記において、原液中の被分離物が多い場
合には中間の開口部35bを開として分離槽23の液面
8をこのレベルとするものである。この開口部35bは
ポンプ22からの吐出液の圧力を利用するシリンダ装置
27により開閉するものであり、電磁弁等よりなる開閉
装置21が制御装置16の指令により開閉し、開閉装置
21が閉のときは、他方の管路の液圧によりシリンダ装
置27のパッキン28が引込まれ、開口部35bが開い
て処理液が流出し、分離槽23の液面8を相応のレベル
とする。
In the above, when there are many substances to be separated in the stock solution, the intermediate opening 35b is opened to bring the liquid level 8 of the separation tank 23 to this level. The opening 35b is opened / closed by a cylinder device 27 that utilizes the pressure of the liquid discharged from the pump 22, and the opening / closing device 21 including an electromagnetic valve opens / closes in response to a command from the control device 16, and the opening / closing device 21 closes. At this time, the packing 28 of the cylinder device 27 is pulled in by the hydraulic pressure of the other pipe line, the opening 35b is opened and the processing liquid flows out, and the liquid level 8 of the separation tank 23 is brought to a suitable level.

【0027】また、開閉装置21が開のときは、シリン
ダ装置27内で弁体30に液圧が作用し、弁体30の左
右に液圧が働く結果、弁棒31を有する側は受圧面積が
少ないため動作圧力が少なく、弁棒31はパッキン28
とともに開口部35bに押つけられ、処理液の流出をと
める。
Further, when the opening / closing device 21 is opened, hydraulic pressure acts on the valve body 30 in the cylinder device 27, and hydraulic pressure acts on the left and right sides of the valve body 30. As a result, the side having the valve rod 31 has a pressure receiving area. Since the operating pressure is low, the valve stem 31 has a packing 28
At the same time, it is pressed against the opening 35b to stop the outflow of the processing liquid.

【0028】上記開口部35bが閉となると、分離槽2
3の液面8は上昇し、開口部35aのレベルに至る。原
液中の被分離物の含有量が若干多い場合には、開口部3
5aは開として液面8をこのレベルに保つが、上記開口
部35aの開閉はシリンダタイプの駆動装置13を駆動
し、同駆動装置13に設けられたパッキンにより行う。
When the opening 35b is closed, the separation tank 2
The liquid level 8 of 3 rises and reaches the level of the opening 35a. When the content of the substance to be separated in the stock solution is slightly high, the opening 3
5a is opened to keep the liquid level 8 at this level, but the opening / closing of the opening 35a is performed by driving a cylinder type drive device 13 and a packing provided in the drive device 13.

【0029】原液中の被分離物の含有量我極めて少い場
合には、上記駆動装置13により開口部35aを閉と
し、分離槽23の液面8を処理液流出管36の開口部の
高さまで上昇させて泡の除去を行い、被分離物を取り除
く。
When the content of the substance to be separated in the stock solution is extremely low, the opening 35a is closed by the driving device 13 and the liquid level 8 of the separation tank 23 is set higher than that of the opening of the processing solution outflow pipe 36. Then, the bubbles are removed by raising the temperature to remove the substance to be separated.

【0030】本実施例においては、分離槽の液面を多段
階にコントロールすることができるため、原液中に含ま
れる被分離物の除去はその濃度のより広範な変化に対応
したものとすることができる。開口部35a、および処
理液流出管36を省略したシステムでも相応の効果を発
揮する。
In this embodiment, since the liquid level in the separation tank can be controlled in multiple stages, the substances to be separated contained in the stock solution should be removed in response to a wider change in the concentration. You can Even in a system in which the opening 35a and the processing liquid outflow pipe 36 are omitted, a corresponding effect is exhibited.

【0031】なお、本発明において、開閉装置は電磁コ
イル、シリンダ装置、ダイヤフラム、エアーバッグ等と
の方法によってもよい。
In the present invention, the opening / closing device may be a method using an electromagnetic coil, a cylinder device, a diaphragm, an air bag or the like.

【0032】[0032]

【発明の効果】本発明においては、気泡発生装置により
発生した気泡に原液中の被分離物を付着して生成された
泡が分離槽の液面の上部に蓄積されると、制御装置から
の制御信号により液面調整手段を作動させて分離槽の液
面を上昇させ、泡除去装置による被分離物が付着した泡
の除去を容易とすることによって、被分離物の濃度変化
に係わらず、被分離物の濃縮効率が高く、被分離物が適
切に除去された処理液の生成が可能な気泡分離装置を実
現する。
According to the present invention, when the bubbles generated by adhering the substance to be separated in the stock solution to the bubbles generated by the bubble generating device are accumulated on the liquid surface of the separation tank, By operating the liquid level adjusting means by the control signal to raise the liquid level in the separation tank and facilitating the removal of the bubbles to which the substances to be separated adhere by the bubble removing device, regardless of the change in the concentration of the substances to be separated, (EN) A bubble separation device having high concentration efficiency of an object to be separated and capable of producing a treatment liquid from which the object to be separated is appropriately removed.

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

【図1】本発明の第1実施例の説明図である。FIG. 1 is an explanatory diagram of a first embodiment of the present invention.

【図2】上記第1実施例の斜視図である。FIG. 2 is a perspective view of the first embodiment.

【図3】本発明の第2実施例の説明図である。FIG. 3 is an explanatory diagram of a second embodiment of the present invention.

【図4】本発明の第3実施例の説明図である。FIG. 4 is an explanatory diagram of a third embodiment of the present invention.

【図5】本発明の第4実施例の説明図である。FIG. 5 is an explanatory diagram of a fourth embodiment of the present invention.

【図6】従来の装置の説明図である。FIG. 6 is an explanatory diagram of a conventional device.

【符号の説明】[Explanation of symbols]

1 分離槽 2 気泡発生装置 3,22 泡除去装置 4 原液流入部 5 処理液流出部 5a 側壁 6 可動堰 7 気泡 8 液面 9 泡 12 処理液流出口 13 駆動装置 14,21 開閉装置 15 駆動源 16 制御装置 17 ガイド 18 モータ 19 回転堰 20 伝達装置 23 蓋付分離槽 24 筒状可動堰 25 処理液流出管 26 処理液濃度モニタ装置 27 シリンダ装置 28 パッキン 29 管路 30 弁体 31 弁棒 33,34 逃がし口 35,36 処理液流出管 DESCRIPTION OF SYMBOLS 1 Separation tank 2 Bubble generator 3,22 Bubble removal device 4 Raw liquid inflow part 5 Processing liquid outflow part 5a Side wall 6 Movable weir 7 Bubbles 8 Liquid level 9 Foam 12 Processing liquid outflow port 13 Driving device 14,21 Opening device 15 Driving source 16 Control device 17 Guide 18 Motor 19 Rotating weir 20 Transmission device 23 Separation tank with lid 24 Cylindrical movable weir 25 Processing liquid outflow pipe 26 Processing liquid concentration monitor device 27 Cylinder device 28 Packing 29 Pipe line 30 Valve body 31 Valve rod 33, 34 Escape port 35, 36 Treatment liquid outflow pipe

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 気泡発生装置と泡除去装置と原液流入部
が設けられた分離槽、同分離槽と内部が連通した処理液
流出部、および同流出部に隣接して設けられた処理液流
出口を備えた気泡分離装置において、上記処理液流出部
に設けられた液面調整手段、および同液面調整手段に接
続された制御装置を備えたことを特徴とする気泡分離装
置。
1. A separation tank provided with a bubble generator, a bubble remover, and a stock solution inflow section, a processing solution outflow section communicating with the separation tank, and a processing solution flow provided adjacent to the outflow section. An air bubble separation device having an outlet, comprising a liquid level adjusting means provided in the treatment liquid outflow portion, and a control device connected to the liquid level adjusting means.
JP3269328A 1991-10-17 1991-10-17 Bubble separation device Expired - Fee Related JP2977341B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3269328A JP2977341B2 (en) 1991-10-17 1991-10-17 Bubble separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3269328A JP2977341B2 (en) 1991-10-17 1991-10-17 Bubble separation device

Publications (2)

Publication Number Publication Date
JPH05103905A true JPH05103905A (en) 1993-04-27
JP2977341B2 JP2977341B2 (en) 1999-11-15

Family

ID=17470832

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3269328A Expired - Fee Related JP2977341B2 (en) 1991-10-17 1991-10-17 Bubble separation device

Country Status (1)

Country Link
JP (1) JP2977341B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4573141B1 (en) * 2009-05-21 2010-11-04 康正 西山 Gas dissolving device
JP2011224422A (en) * 2010-04-15 2011-11-10 Yanmar Co Ltd Foam separation apparatus
KR101119640B1 (en) * 2011-03-30 2012-03-16 (주)에스엠워터테크 Micro bubble filtering apparatus
CN102633317A (en) * 2012-04-17 2012-08-15 江苏南方涂装环保股份有限公司 Rapid liquid level regulator for air floatation device
KR20190039003A (en) * 2017-10-02 2019-04-10 스미또모 가가꾸 가부시키가이샤 Method for producing polyvinyl alcohol-based resin film
JP2019066838A (en) * 2017-10-02 2019-04-25 住友化学株式会社 Method for manufacturing polyvinyl alcohol resin film

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4573141B1 (en) * 2009-05-21 2010-11-04 康正 西山 Gas dissolving device
JP2010269299A (en) * 2009-05-21 2010-12-02 Yasumasa Nishiyama Gas dissolving apparatus
JP2011224422A (en) * 2010-04-15 2011-11-10 Yanmar Co Ltd Foam separation apparatus
KR101119640B1 (en) * 2011-03-30 2012-03-16 (주)에스엠워터테크 Micro bubble filtering apparatus
CN102633317A (en) * 2012-04-17 2012-08-15 江苏南方涂装环保股份有限公司 Rapid liquid level regulator for air floatation device
KR20190039003A (en) * 2017-10-02 2019-04-10 스미또모 가가꾸 가부시키가이샤 Method for producing polyvinyl alcohol-based resin film
JP2019066838A (en) * 2017-10-02 2019-04-25 住友化学株式会社 Method for manufacturing polyvinyl alcohol resin film

Also Published As

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