JPH0471687A - Water treating device using ozone and defoaming method thereof - Google Patents

Water treating device using ozone and defoaming method thereof

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Publication number
JPH0471687A
JPH0471687A JP18115890A JP18115890A JPH0471687A JP H0471687 A JPH0471687 A JP H0471687A JP 18115890 A JP18115890 A JP 18115890A JP 18115890 A JP18115890 A JP 18115890A JP H0471687 A JPH0471687 A JP H0471687A
Authority
JP
Japan
Prior art keywords
water
tank
contact tank
flow control
control plate
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
Application number
JP18115890A
Other languages
Japanese (ja)
Inventor
Nobuyuki Motoyama
信行 本山
Takayuki Morioka
崇行 森岡
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP18115890A priority Critical patent/JPH0471687A/en
Publication of JPH0471687A publication Critical patent/JPH0471687A/en
Pending legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To efficiently remove the foam generated in a contact tank by mounting a water flow control plate to the water treating device having a flow regulating tank and the contact tank 18 and controlling the water flow from the flow regulating tank to the contact tank. CONSTITUTION:The water flow control plate 21 having an inclination with a water surface is mounted slight apart from the water surface near the partition plate 16 in the contact tank 18. The water 2 to be treated flowing into a reaction tank 1 collides against the water flow control plate 21 and flows down along the partition plate 16 to the contact tank 18. On the other hand, the passage rate of the ozonizing air from an air diffusion pipe 11a is decreased and the passage rate of the ozonizing air from an air diffusion pipe 11b is increased, to generate swirling flow in the water 2 to be treated in the contact tank 18. The bubbles 20 accumulating on the water surface are moved to the place of the water flow control plate 21 by this swirling flow and are thereafter withdrawn into the contact tank 18 together with the water 2 to be treated flowing into the spacing between the water flow control plate 21 and the partition plate 16. Then, the stagnation of the bubbles in the space part 16 is obviated.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はオゾンを用いた上水や下水の高度処理や工場廃
水処理など比較的規模の大きい水処理装置と、被処理水
とオゾンの反応によって生ずる泡の消泡方法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to relatively large-scale water treatment equipment, such as advanced treatment of water and sewage and factory wastewater treatment, using ozone, and the reaction between water to be treated and ozone. This invention relates to a method for defoaming foam caused by.

〔従来の技術〕[Conventional technology]

オゾンを用いた水処理装置における被処理水と造がとら
れているが、上下水処理をはじめ規模の大きい装置では
、反応工学的な見地からオゾンと被処理水が対向流で接
触する向流接触方式の反応槽が用いられる場合が多い。
Ozone is used as the treated water in water treatment equipment, but in large-scale equipment such as water and sewage treatment, from the viewpoint of reaction engineering, ozone and treated water come into contact with each other in countercurrent flow. A contact type reaction tank is often used.

第3図はこのような水処理装置の要部構成の一例を示し
た模式図である。第3図において、反応槽1には被処理
水2がタンク3からポンプ4により被処理水人口5を通
って供給され、処理水出口6から流出される。この際、
コンプレッサ7を用いて加圧空気をオゾン発生器8に送
り、生成したオゾン化空気が例えば2経路に別れて流量
調節弁9a、9b流量計10a、 10bを経て散気管
11a、llbにより反応槽l内に注入、拡散されて被
処理水2と反応する0反応に関与しなかった排オゾンは
、反応槽lの上部の排オゾン出口12から出て配管13
を通り、処理塔14に導かれここで酸素に分解される。
FIG. 3 is a schematic diagram showing an example of the main part configuration of such a water treatment device. In FIG. 3, treated water 2 is supplied to the reaction tank 1 from a tank 3 by a pump 4 through a treated water volume 5, and is discharged from a treated water outlet 6. On this occasion,
Pressurized air is sent to the ozone generator 8 using the compressor 7, and the generated ozonized air is divided into two routes, for example, passes through flow rate control valves 9a, 9b, flow meters 10a, 10b, and is then sent to the reaction tank l by aeration pipes 11a, llb. Exhaust ozone that does not participate in the reaction that is injected and diffused into the reactor and reacts with the water to be treated 2 exits from the exhaust ozone outlet 12 at the top of the reaction tank l and is transferred to the pipe 13.
, and is led to the treatment tower 14 where it is decomposed into oxygen.

同時に徘オゾンは、その一部が配管13の途中に分岐し
て設けられたオゾン濃度測定器15に採取される。
At the same time, a part of the wandering ozone is collected by an ozone concentration measuring device 15 installed in a branch part of the pipe 13.

また反応槽1内は幾つかの仕切り板16で分割され、大
別するとポンプ4によって輸送された被処理水2を流入
部において整流させる整流槽17と、その後段で底部に
等間隔に配置した散気管11a、11bによりオゾンの
微細気泡を拡散させる接触槽18とからなっている。矢
印は水流の方向を示す。
The inside of the reaction tank 1 is divided by several partition plates 16, and roughly divided into a rectifier tank 17 that rectifies the water to be treated 2 transported by the pump 4 at the inlet, and a rectifier tank 17 that rectifies the water 2 transported by the pump 4 at the inlet, and a rectifier tank 17 that is arranged at equal intervals at the bottom in the subsequent stage. It consists of a contact tank 18 in which fine ozone bubbles are diffused by aeration pipes 11a and 11b. Arrows indicate the direction of water flow.

このような装置により水処理を実施するとき、発泡性の
ある被処理水2を処理する場合は、オゾンとの反応によ
って泡や固形分などが水面に浮上し、これらが水面と反
応槽1内の上壁との間に形成される空間部19に蓄積さ
れてしまう、第4図はその様子を示した模式図であり、
反応槽lとオゾン供給系統の一部のみをやや拡大して示
しである。
When water treatment is carried out using such a device, when treating water 2 with foaming properties, foams and solids rise to the surface of the water due to the reaction with ozone, and these are mixed between the water surface and the inside of the reaction tank 1. FIG. 4 is a schematic diagram showing this situation, and is accumulated in the space 19 formed between the upper wall and the upper wall.
Only a portion of the reaction tank 1 and the ozone supply system are shown slightly enlarged.

第4図の如く発泡性のある被処理水2では、その水面上
に泡20が滞留するようになる。この状態になると、排
オゾンは配管13を流れ難くなり、また反応槽1の内圧
の変化に伴なう水位の変動やオゾンの注入量の低下など
を生ずる。さらに、泡が処理塔14やオゾン濃度測定器
15に達し、これらの性能低下や故障を起こさせる。こ
れに対して一般的な消泡対策として、従来、水や空気な
どの吹き付けまたは機械的、熱的な方法、その他消泡剤
を用いるなどの方法が行われている。
In the treated water 2 having foaming properties as shown in FIG. 4, bubbles 20 stay on the water surface. In this state, it becomes difficult for exhaust ozone to flow through the pipe 13, and the water level fluctuates and the amount of ozone injected decreases due to changes in the internal pressure of the reaction tank 1. Furthermore, the bubbles reach the treatment tower 14 and the ozone concentration measuring device 15, causing a decrease in their performance or failure. To deal with this, conventional defoaming measures include spraying water, air, etc., mechanical, thermal methods, and other methods such as using defoaming agents.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、上記の消泡対策は、いずれも決定的な効
果に欠け、特に上水処理ではこれまでに殆ど実績がなく
、さらに次のような制約もある。
However, all of the antifoaming measures described above lack decisive effects, and in particular, there has been little experience so far in water treatment, and furthermore, they have the following limitations.

■空気を送ると排オゾンの処理塔14の負荷が増大する
(2) When air is sent, the load on the exhaust ozone treatment tower 14 increases.

■上水道であるから一度実施した後は給水を止められす
、複雑な構造を持つ機械的、熱的な消泡装置は使用する
ことができない。
■Since it is a water supply, the water supply cannot be stopped once it has been applied, and mechanical and thermal defoaming devices with complicated structures cannot be used.

■上水道には消泡剤など薬品を用いることができない。■ Chemicals such as antifoaming agents cannot be used in water supplies.

■季節によって泡の発生の程度が異なり、冬季の渇水期
を除いては発泡しないこともあるので、保管管理上の問
題もある。
■The degree of foaming varies depending on the season, and it may not foam at all except during the winter dry season, which poses storage management problems.

本発明は上述の点に鑑みてなされたものであり、その目
的はオゾンによる水処理装置に発生し接触槽内に滞留す
る泡を効率よく除去するための装置と方法を提供するこ
とにある。
The present invention has been made in view of the above points, and its object is to provide an apparatus and method for efficiently removing foam generated in an ozone water treatment apparatus and retained in a contact tank.

〔課題を解決するための手段〕[Means to solve the problem]

上記の課題を解決するために、水処理装置の整流槽と接
触槽を区分する仕切り板の接触槽側近傍に、水面と僅か
な隙間を保ち水面に対して傾斜を有する水流制御板を取
り付けた構造とし、2系列の散気管を用いて通気量を一
方は小さく他方は大きくして、接触槽内の被処理水に旋
回流を起こさせることにより、水面上に浮上し滞留する
泡をこの旋回流によって水流制御板の位置まで移動させ
、被処理水が水位の高い整流槽から水位の低い接触槽へ
流入するときに、水流制御板に沿って泡を接触槽内に落
とし込むようにしたものである。
In order to solve the above problem, we installed a water flow control plate that maintains a small gap with the water surface and is inclined with respect to the water surface near the contact tank side of the partition plate that separates the rectification tank and contact tank of the water treatment equipment. This structure uses two series of aeration pipes, one with a small aeration volume and one with a large aeration volume, to create a swirling flow in the water to be treated in the contact tank. The bubbles are moved by the current to the position of the water flow control plate, and when the water to be treated flows from the rectifier tank with a high water level to the contact tank with a low water level, the bubbles are dropped into the contact tank along the water flow control plate. be.

〔作用〕[Effect]

上記の装置構成と消泡方法により、接触槽内に発生する
泡は水面上に浮上したとき、被処理水の旋回流によって
遂次水流制御板の方向に押し流されるとともに、整流槽
から流れてきて水流制御板に衝突する水流で接触槽内に
引きずり込まれてしまうので、反応槽内の空間部には常
に泡の滞留を生ずることがない。
With the above equipment configuration and defoaming method, when the bubbles generated in the contact tank rise to the surface of the water, they are successively swept away in the direction of the water flow control board by the swirling flow of the water to be treated, and also flow from the rectifier tank. Since the bubbles are dragged into the contact tank by the water flow that collides with the water flow control plate, bubbles do not always remain in the space inside the reaction tank.

〔実施例〕〔Example〕

以下、本発明を実施例に基づき説明する。 Hereinafter, the present invention will be explained based on examples.

第1図は本発明の適用される水処理装置の要部構成を示
した模式図であり、第3図と共通部分を同一符号で表わ
しである。第1図が第3図と異なる所は、接触槽18内
の仕切り板16の近傍に、水面からやや離れて水面に対
して傾斜を持つ水流制御板21を反応槽1に取り付けた
ことである。その他の構成は第3図と同じであるからそ
の説明は省略する。
FIG. 1 is a schematic diagram showing the main structure of a water treatment apparatus to which the present invention is applied, and parts common to those in FIG. 3 are represented by the same symbols. The difference between FIG. 1 and FIG. 3 is that a water flow control plate 21 is attached to the reaction tank 1 near the partition plate 16 in the contact tank 18, slightly away from the water surface and inclined to the water surface. . The rest of the configuration is the same as that in FIG. 3, so a description thereof will be omitted.

第2図は水流制御板21を有する第1図の装置の反応槽
1とオゾン供給系統の一部のみを示した模式図であり、
第4図と比較対応するものである。
FIG. 2 is a schematic diagram showing only a part of the reaction tank 1 and ozone supply system of the apparatus of FIG. 1 having a water flow control plate 21,
It corresponds to FIG. 4 for comparison.

第2図において、整流槽17と接触槽18との間の仕切
り板16によって整流槽17の方が接触槽18より水位
が高くなるようにしであるので、反応[1に流入する被
処理水2は、整流槽17を通り接触槽18に流れ込むの
であるが、このとき被処理水2は水流制御板12に衝突
することにより、仕切り板16に沿って接触槽18に流
れ落ちるようになる。そこで、流量調節弁9aを絞り、
散気管11aからのオゾン化空気の通気量を小さくし、
さらに流量調節弁9bを開き散気管11bからのオゾン
化空気の通気量を大きくすることによって、接触槽18
内の被処理水2に矢印のような旋回流を生じさせる。
In FIG. 2, the water level in the rectifier tank 17 is higher than that in the contact tank 18 due to the partition plate 16 between the rectifier tank 17 and the contact tank 18. flows into the contact tank 18 through the rectifier tank 17, but at this time, the water to be treated 2 collides with the water flow control plate 12, so that it flows down into the contact tank 18 along the partition plate 16. Therefore, the flow rate control valve 9a is throttled down.
The ventilation amount of ozonized air from the aeration pipe 11a is reduced,
Further, by opening the flow rate control valve 9b and increasing the amount of ozonized air flowing from the aeration pipe 11b, the contact tank 18
A swirling flow as shown by the arrow is generated in the water to be treated 2 inside.

このようにしたときの泡の状態を第4図と比較すると、
第4図で水面上に溜まった泡20は、この位置から接触
槽18内の旋回流によって第2図の位置即ち水流制御板
21の個所まで移動するようになる。ここで泡20は水
流制御板21と仕切り板16との隙間に流れ込む被処理
水2とともに、接触槽18内に引きずり込まれてしまう
ので、空間部19に泡が滞留することがなくなる。かく
して排オゾンを支障なく配管13に送ることができ、そ
の他泡の発生に関わる不都合な事態は解消されるのであ
る。
Comparing the state of the bubbles when doing this with Figure 4, we find that
The bubbles 20 accumulated on the water surface in FIG. 4 are moved from this position to the position shown in FIG. 2, that is, the water flow control plate 21, by the swirling flow in the contact tank 18. Here, the bubbles 20 are dragged into the contact tank 18 together with the water to be treated 2 flowing into the gap between the water flow control plate 21 and the partition plate 16, so that the bubbles do not stay in the space 19. In this way, the exhausted ozone can be sent to the pipe 13 without any hindrance, and other inconvenient situations related to the generation of bubbles are eliminated.

〔発明の効果〕〔Effect of the invention〕

上水処理をはじめ大規模な反応槽を用いてこれにオゾン
を通気し水処理を行なうとき、従来反応槽内に発生する
泡を除去する有効な手段がなかったが、本発明では実施
例で述べたように、オゾン化空気を接触槽に通気する2
系統の散気管の通気量を変えて被処理水に旋回流を起こ
させて、水面上に浮上しそこに溜まる泡を、整流槽と接
触槽に水位差をつけて被処理水を落とし込む傾斜付きの
水流制御板の位置に集め、この泡を水流制御板に沿って
接触槽内に引き入れるようにしたために、水処理工程中
に水面に泡が滞留することなく、泡の発生に起因する種
々の不都合を解消し、簡単な水流制御板の付設と、オゾ
ン化空気を接触槽に通気するときの簡単なバルブ操作だ
けで、保守管理の容易な極めて効果的な消泡を行なうこ
とができる。
Conventionally, there was no effective means for removing bubbles generated in the reaction tank when a large-scale reaction tank was used for water treatment, such as water treatment, by aerating ozone into the tank. As mentioned, venting ozonated air into the contact tank2
A sloping system that creates a swirling flow in the water to be treated by changing the airflow rate of the air diffuser pipe in the system, removes the bubbles that float to the surface of the water and accumulate there, and drops the water into the rectifier tank and the contact tank with a water level difference. Since the bubbles are collected at the water flow control plate position and drawn into the contact tank along the water flow control plate, the bubbles do not remain on the water surface during the water treatment process, and various types of bubbles caused by the generation of bubbles are eliminated. By eliminating these inconveniences and simply installing a water flow control plate and operating a simple valve when venting ozonated air into the contact tank, extremely effective defoaming can be achieved with easy maintenance.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の通用される水処理装置の要部構成を示
した模式図、第2図は本発明の装置の反応槽とオゾン供
給系統の一部を示した模式図、第3図は従来の水処理装
置の要部構成を示した模式図、第4図は従来の水処理装
置の反応槽とオゾン供給系統の一部を示した模式図であ
る。 1:反応槽、2:被処理水、3:タンク、4:ポンプ、
5:被処理水入口、6:処理水出口、7:コンプレッサ
、8ニオシン発生器、9a、9b  :流量調節弁、1
0a、10b :流量針、11a、11b  :散気管
、12:排オゾン出口、13:配管、14:処理塔、1
5ニオシン濃度測定器、16:仕切り板、17:整流槽
、18:接触槽、19:空間部、20:泡、21:水流
第2図 lA3肥 第4図
Fig. 1 is a schematic diagram showing the main part configuration of the water treatment equipment of the present invention, Fig. 2 is a schematic diagram showing a part of the reaction tank and ozone supply system of the equipment of the present invention, and Fig. 3 4 is a schematic diagram showing the main part configuration of a conventional water treatment device, and FIG. 4 is a schematic diagram showing a part of the reaction tank and ozone supply system of the conventional water treatment device. 1: Reaction tank, 2: Water to be treated, 3: Tank, 4: Pump,
5: Treated water inlet, 6: Treated water outlet, 7: Compressor, 8 Niosin generator, 9a, 9b: Flow rate control valve, 1
0a, 10b: flow needle, 11a, 11b: diffuser pipe, 12: exhaust ozone outlet, 13: piping, 14: treatment tower, 1
5 Niosin concentration measuring device, 16: Partition plate, 17: Rectifier tank, 18: Contact tank, 19: Space, 20: Foam, 21: Water flow diagram 2 lA3 fertilizer diagram 4

Claims (1)

【特許請求の範囲】 1)仕切り板によって区分された高水位の整流槽と低水
位の接触槽を持つ反応槽の前記接触槽底部に配置した散
気管からオゾン化空気を注入して前記反応槽内を流通す
る廃水を処理する装置の前記仕切り板近傍の前記接触槽
領域に、前記整流槽から流入する被処理水が衝突して前
記接触槽内に流れ込む傾斜を有するとともに前記接触槽
の水面と隙間を保つ水流制御板を備えたことを特徴とす
るオゾンを用いた水処理装置。 2)請求項1)記載の水処理装置に発生する泡を除去す
るに当たり、2系列の散気管を配置しオゾン化空気の通
気量を一方は小さく他方は大きくして前記接触槽内の被
処理水に旋回流を生じさせ、前記接触槽の水面上に浮上
し滞留する泡を前記旋回流によって水流制御板の位置ま
で移動させるとともに前記接触槽内に引き入れることを
特徴とするオゾンを用いた水処理装置の消泡方法。
[Claims] 1) Ozonated air is injected into the reaction tank from an aeration pipe arranged at the bottom of the contact tank of a reaction tank having a high water level rectifying tank and a low water level contact tank separated by a partition plate. The contact tank area near the partition plate of the apparatus for treating wastewater flowing therein has an inclination such that the water to be treated flowing from the rectifying tank collides and flows into the contact tank, and the water surface of the contact tank A water treatment device that uses ozone and is characterized by being equipped with a water flow control plate that maintains gaps. 2) In removing bubbles generated in the water treatment apparatus according to claim 1), two series of aeration pipes are arranged, and the amount of ozonized air is made small in one direction and large in the other, so that the amount of ozonized air to be treated in the contact tank is Water using ozone, characterized in that a swirling flow is generated in water, and bubbles floating and staying on the water surface of the contact tank are moved to a position of a water flow control plate and drawn into the contact tank by the swirling flow. Defoaming method for processing equipment.
JP18115890A 1990-07-09 1990-07-09 Water treating device using ozone and defoaming method thereof Pending JPH0471687A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18115890A JPH0471687A (en) 1990-07-09 1990-07-09 Water treating device using ozone and defoaming method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18115890A JPH0471687A (en) 1990-07-09 1990-07-09 Water treating device using ozone and defoaming method thereof

Publications (1)

Publication Number Publication Date
JPH0471687A true JPH0471687A (en) 1992-03-06

Family

ID=16095905

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18115890A Pending JPH0471687A (en) 1990-07-09 1990-07-09 Water treating device using ozone and defoaming method thereof

Country Status (1)

Country Link
JP (1) JPH0471687A (en)

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