JPS63104697A - Apparatus for producing ozone dissolved water - Google Patents

Apparatus for producing ozone dissolved water

Info

Publication number
JPS63104697A
JPS63104697A JP25121286A JP25121286A JPS63104697A JP S63104697 A JPS63104697 A JP S63104697A JP 25121286 A JP25121286 A JP 25121286A JP 25121286 A JP25121286 A JP 25121286A JP S63104697 A JPS63104697 A JP S63104697A
Authority
JP
Japan
Prior art keywords
ozone
water
pipe
water supply
dissolution tank
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
JP25121286A
Other languages
Japanese (ja)
Inventor
Kenzo Watanabe
健三 渡辺
Eiji Sakai
英治 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.)
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 JP25121286A priority Critical patent/JPS63104697A/en
Publication of JPS63104697A publication Critical patent/JPS63104697A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To easily produce ozone dissolved water having a high ozone concn. by forming the circulating flow which returns the ozone dissolved water stored in a storage tank via a reflux pipe and feed pipe to a dissolution tank and feeding fresh ozonizing gas to the water. CONSTITUTION:A water feed pump 2, a 1st ejector 5, a 2nd ejector 6 and a check valve 16 are interposed in series to the water feed pipe 9 to the dissolution tank 1 which is a hermetic vessel equipped with a discharge pipe 13 having a drain valve 12. The pump 2 is driven to feed the ozonizing gas from an ozone generator 4 via the ejector 5 into the feed water to dissolve the ozone incorporated therein. The undissolved ozonizing gas stagnating in the tank 1 is further fed to the ejector 6 and is incorporated into the feed water. The reflux pipe 14 communicating the discharge pipe 13 and the feed pipe 9 is provided to form the circulating flow to return the ozone dissolved water stored in the storage tank through the reflux pipe 14 and the feed pie 9 to the dissolution tank so that the fresh ozonizing gas is fed into the water. The ozone dissolved water having the high ozone concn. is thereby easily produced.

Description

【発明の詳細な説明】 〔発明の属する技術分野〕 この発明は、空気又は酸素を原料とするオゾン用のオゾ
ン溶解水製造装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical field to which the invention pertains] This invention relates to an apparatus for producing ozone-dissolved water using air or oxygen as a raw material.

〔従来技術とその問題点〕[Prior art and its problems]

この種の装置としては、上水道施設や排水処理施設にお
ける浄化設備として大容量のオゾン発生装置で得られる
高濃度、高圧のオゾン化ガスを高圧のブロアを利用して
吹き込ませる方式の大容量のものは存在しているが、最
近殺菌、脱臭、脱色などを目的とする民生用装置として
、小容量、低圧力のオゾン発生装置からのオゾン化ガス
を用いてオゾン溶解水を製造する装置の普及が見られる
が、しかしこの目的のためによい方法が確立されている
とは言えないのが実情である。
This type of device is a large-capacity device that uses a high-pressure blower to blow high-concentration, high-pressure ozonized gas obtained from a large-capacity ozone generator as purification equipment in water supply facilities and wastewater treatment facilities. However, recently, devices that produce ozone-dissolved water using ozonized gas from small-capacity, low-pressure ozone generators have become popular as consumer devices for purposes such as sterilization, deodorization, and decolorization. However, the reality is that no good method has been established for this purpose.

以下図面に基づいてその点を説明する。第4図ないし第
6図はいずれも従来装置の概略を示す構成図である。
This point will be explained below based on the drawings. 4 to 6 are configuration diagrams showing the outline of the conventional device.

第4図は、上部が開放されている溶解槽1の底部に散気
ディフューザ24を設置し、その散気ディフューザ24
とオゾン発生装置4とをオゾン送出管10で連通させ、
オゾン化ガスを水中に放散し該ガスが溶解槽1内の水中
を気泡となって上昇する間にオゾンを水に溶解させるよ
うに構成されたもので、排出弁23を開閉してオゾン溶
解水を取出す方式のものである。この場合充分な濃度の
オゾン溶解水とするには、気泡の水中での滞留時間が大
きい程良いため、溶解槽の水深を深くし装置が大きくな
り勝ちであるが、あまり深いとオゾン化ガスの圧力が低
いため逆流するおそれがあるので深くできないといった
問題や未溶解オゾンを含むオゾン化ガスを大気中に放散
する恐れがあるといった欠点がある。
FIG. 4 shows an air diffuser 24 installed at the bottom of the melting tank 1 whose top is open, and the air diffuser 24
and the ozone generator 4 through an ozone delivery pipe 10,
It is configured to dissipate ozonized gas into the water and dissolve the ozone in the water while the gas rises in the form of bubbles in the water in the dissolution tank 1, and the discharge valve 23 is opened and closed to release the ozone-dissolved gas. It is a type of extraction method. In this case, in order to obtain ozone-dissolved water with a sufficient concentration, the longer the residence time of the bubbles in the water, the better. Therefore, the water depth of the dissolution tank should be made deeper and the equipment likely to be larger, but if the water is too deep, the ozonized gas There are disadvantages such as the problem that the pressure is low and it is impossible to go deep because there is a risk of backflow, and there is a risk that ozonized gas containing undissolved ozone will be released into the atmosphere.

第5図は、給水ポンプ2の上流側でオゾン発生装置4に
接続するオゾン送出管10を給水管9に接続し、給水ポ
ンプ2の駆動にしたがって給水管9中を流れる給水にオ
ゾン発生装置4から直接オゾン化ガスを混入溶解させ使
用するように構成したもので、給水ポンプ2が駆動され
該ポンプ2に吸い込まれる水にオゾン化ガスを混入させ
オゾン溶解水を得るという方式であるためオゾン化ガス
の水中での滞留時間が短かくオゾンの溶は込みが充分で
ない上、未溶解のオゾンが放出され環境を害しやすいと
いった問題があり、また給水ポンプの耐オゾン性も大き
な問題となりやすい。
FIG. 5 shows that an ozone delivery pipe 10 connected to the ozone generator 4 on the upstream side of the water supply pump 2 is connected to the water supply pipe 9, and the ozone generator 4 is connected to the supply water flowing through the water supply pipe 9 as the water supply pump 2 is driven. The water supply pump 2 is driven and the ozonated gas is mixed into the water sucked into the pump 2 to obtain ozonated water. There are problems in that the residence time of gas in water is short and ozone is not sufficiently dissolved, and undissolved ozone is easily released and harms the environment.Additionally, the ozone resistance of the water pump tends to be a major problem.

第6図は、密閉容器である溶解槽1と給水ポンプ2との
間にエゼクタ5を配し、その吸入口にオゾン送出管10
を接続し、給水ポンプ2を駆動して溶解槽1の下方から
溶解槽1へ水を給水する際の水の力を利用して、オゾン
発生装置4からのオゾン化ガスを流水中に取込ませ拡拌
しながら溶解槽1へ送り、さらに気泡となって上昇する
間にオゾンを溶解させるように構成したもので、水中で
のオゾン化ガスの滞留時間は十分とれ比較的高譲度のオ
ゾン溶解水が得られる効果があるとしても、給水ポンプ
がg動している間しかオゾン化ガスを取り込めないこと
、密閉容器であるので空気抜きを設けて常に一定量の水
が溶解槽に貯留されるようにしておくこと、又連続して
使用される場合。
In FIG. 6, an ejector 5 is arranged between the dissolution tank 1, which is a closed container, and the water supply pump 2, and an ozone delivery pipe 10 is placed at the inlet of the ejector 5.
The ozonized gas from the ozone generator 4 is taken into the flowing water by connecting the water supply pump 2 and using the power of water when supplying water from below the dissolution tank 1 to the dissolution tank 1. This system is configured so that the ozone gas is sent to the dissolution tank 1 while being expanded, and the ozone is dissolved while it rises in the form of bubbles.The residence time of the ozonized gas in the water is sufficient, and the ozone has a relatively high yield. Even if there is an effect of obtaining dissolved water, the ozonized gas can only be taken in while the water pump is in motion, and since it is a closed container, an air vent is provided so that a certain amount of water is always stored in the dissolving tank. If the product is used continuously or if it is used continuously.

オゾン化ガスの滞留時間が不十分となりやすく、かつ未
溶解オゾンの放出という問題もある。
There is also the problem that the residence time of the ozonized gas tends to be insufficient and that undissolved ozone is released.

以上3つの事例に共通していることは、オゾン溶解水の
オゾン濃度をオゾン化ガスの滞留時間が短かいため余り
高(することができないということと、未溶解オゾンが
大気中に放出されるといった欠点である。
What the above three cases have in common is that the ozone concentration in the ozone-dissolved water cannot be raised too high due to the short residence time of the ozonized gas, and undissolved ozone is released into the atmosphere. This is a drawback.

〔発明の目的〕[Purpose of the invention]

本発明は上記の諸点を勘fi−シてなされたもので、浴
解しきれなかったオゾンを含むオゾン化ガスの大気中へ
の放散をなくするととも番こ、低圧力のオゾン発生装置
であっても高譲度のオゾン溶解水が得られるコンパクト
なオゾン溶解水製造装置を提供することを目的とする。
The present invention has been made with the above points in mind, and is a low-pressure ozone generator that eliminates the release of ozonized gas containing undissolved ozone into the atmosphere. It is an object of the present invention to provide a compact ozone-dissolved water producing device capable of producing ozone-dissolved water with a high yield even when the water is used.

〔発明の要旨〕[Summary of the invention]

上記目的は本発明によれば、オゾン発生装置と。 According to the present invention, the above object provides an ozone generator.

オゾンを溶解し貯留する溶解槽と、給水ポンプ。A dissolution tank that dissolves and stores ozone and a water pump.

第1エゼクタ、第2エゼクタ及び逆上弁を介装し前記溶
解槽に接続される給水管と、排出弁を備え前記溶解槽内
のオゾン溶解水を送出する排出管と、前記溶解槽内に滞
留するオゾン化ガスを抽出し前記第2エゼクタの送流す
るオゾン環流管と、前記滞留オゾン化ガスの圧力が設定
値を超過したら電気信号を出力する圧力スイッチと、該
圧力スイッチの電気信号で開閉が制御される電磁弁とオ
ゾン接触分解器とを介装している放出管と、前記溶解槽
内の水位が設定値からはずれたら電気信号を出力するレ
ベルスイッチとを配備するとともに、前記排出弁の上流
側で排出管から分岐し給水ポンプの上流側で給水管に接
続される電磁弁を備えている環流管と、オゾン発生装置
から出たオゾン化ガスを第1エゼクタへ送流するオゾン
送出管とから形成され、オゾン溶解水の送出に応動して
排出弁及びオゾン送出管との電磁弁の開閉と、給水ポン
プの駆動モータならびにオゾン発生装置の駆動とを制御
し、さらにレベルスイッチの電気信号によって環流管及
びオゾン送出管との電磁弁の開閉と給水ポンプの駆動モ
ータならびiこオゾン発生装置の駆動とが制御されるよ
うにすることによって達成される。
A water supply pipe that is connected to the dissolution tank through a first ejector, a second ejector, and a reverse valve; a discharge pipe that is equipped with a discharge valve and that sends out the ozone-dissolved water in the dissolution tank; an ozone reflux pipe that extracts the accumulated ozonized gas and sends it to the second ejector; a pressure switch that outputs an electric signal when the pressure of the accumulated ozonized gas exceeds a set value; and an electric signal from the pressure switch. A discharge pipe is equipped with a solenoid valve whose opening/closing is controlled and an ozone catalytic decomposer, and a level switch which outputs an electric signal when the water level in the dissolution tank deviates from a set value. A reflux pipe equipped with an electromagnetic valve that branches from the discharge pipe on the upstream side of the valve and is connected to the water supply pipe on the upstream side of the water supply pump, and an ozone pipe that sends the ozonized gas discharged from the ozone generator to the first ejector. In response to the delivery of ozone dissolved water, it controls the opening and closing of the discharge valve and the solenoid valve connected to the ozone delivery pipe, the drive motor of the water supply pump, and the drive of the ozone generator, and also controls the operation of the level switch. This is achieved by controlling the opening and closing of electromagnetic valves connected to the reflux pipe and the ozone delivery pipe, the drive motor of the water supply pump, and the drive of the ozone generator using electric signals.

〔発明の実施例〕[Embodiments of the invention]

以下本発明を適用した実施例の図面に基づいて説明する
。第1図は実施例のオゾン溶解水製造の概略を示す構成
図で、第2図及び第3図はともに他の実施例のオゾン溶
解水製造装置の概略構成図である。
Embodiments to which the present invention is applied will be described below based on the drawings. FIG. 1 is a block diagram showing an outline of ozone-dissolved water production according to an embodiment, and FIGS. 2 and 3 are both schematic diagrams of an ozone-dissolved water producing apparatus according to another embodiment.

第1図において、1は密閉容器につくられた溶解槽であ
って、図示しない給水源から給水管9を介して核種の下
方から給水されるようになっており、核種1の側壁化は
電磁弁である排出弁12が配備されている排出管13が
接続されていて、排出弁12の開放によって図示しない
供給先へイオン溶解水が送出されるようになっている。
In Fig. 1, numeral 1 is a dissolution tank made in a closed container, and water is supplied from below the nuclide from a water supply source (not shown) through a water supply pipe 9, and the side wall of the nuclide 1 is electromagnetic. A discharge pipe 13 equipped with a discharge valve 12 is connected thereto, and when the discharge valve 12 is opened, ion-dissolved water is sent to a supply destination (not shown).

また給水管′9には電気信号によって駆動が制御される
給水ポンプ駆動用電動機(以下駆動モータという)3が
直結している給水ポンプ2と、給水ポンプ2を経てきた
加圧給水によって駆動され、その吸込口に電磁弁8を介
装しているオゾン送出管1oを接続している第1エゼク
タ5と、第1エゼクタ5から吐出された加圧給水によっ
て駆動され、その吸込口に溶解槽1内1こ滞留するオゾ
ン化ガスを抽出し送流するオゾン環流管11が接続され
ている第2エゼクタ6と、逆止弁16とが、上記の屓に
直列に介装されている。オゾン送出管1oは一端がオゾ
ン発生装ft4に接続され他端が電磁弁8を介して第1
エゼクタ5の吸込口に接続している。
Further, the water supply pipe '9 is driven by a water supply pump 2 directly connected to a water supply pump driving electric motor (hereinafter referred to as a drive motor) 3 whose drive is controlled by an electric signal, and the pressurized water supplied through the water supply pump 2. A first ejector 5 is connected to an ozone delivery pipe 1o with a solenoid valve 8 interposed in its suction port, and a dissolution tank 1 is driven by the pressurized water discharged from the first ejector 5. A second ejector 6 to which an ozone reflux pipe 11 for extracting and sending the ozonized gas retained in the second ejector 6 and a check valve 16 are interposed in series on the above-mentioned bottom. One end of the ozone delivery pipe 1o is connected to the ozone generator ft4, and the other end is connected to the first ozone generator via the solenoid valve 8.
It is connected to the suction port of the ejector 5.

したがって給水ポンプ2及びオゾン発生装置4が駆動し
、電磁弁8が開ならば、給水管9内を加圧給水が流れ、
第1エゼクタ5はオゾン発生装置4からオゾン送出管l
Oを介して供給されるオゾン化ガスを該給水中へ取り込
み気泡として流し、第2エゼクタ6、逆上弁16を介し
て溶解槽1に至り、該溶解槽l内に貯留する液中を上昇
する間に該ガス中のオゾンが水に溶は込みオゾン溶解水
が生成される。一方オシン化ガスの未溶解部分は溶解槽
1の上部に滞留するが、それはオゾン環流管11を介し
て第2エゼクタ6へ送られ、再び給水管9内を流れる加
圧給水中に取り込まれ逆上弁16を介して溶解槽1へ橋
流し、その中のオゾンが液中にとり込まれるように循環
するのである。さらに溶解槽1には、その排出管13の
排出弁12の上流側で排出管13から分岐し、かつその
分流直後に電磁弁15を介装し、終端が給水管9の給水
ポンプ2の上流側に接続されている環流管14が配備さ
れている。したがって排出弁13が閉または僅かに開で
電磁弁15が開の状況で給水ポンプ2が駆動していると
、溶解槽1内のイオン溶解水は環流管14を介して給水
管9へ戻りさらに給水ポンプ21によって溶解・槽1へ
環流する循環流を生ずるよう番こなる。
Therefore, when the water supply pump 2 and the ozone generator 4 are driven and the solenoid valve 8 is opened, pressurized water flows through the water supply pipe 9.
The first ejector 5 is an ozone delivery pipe l from the ozone generator 4.
The ozonized gas supplied through O is taken into the water supply and flows as bubbles, reaches the dissolution tank 1 via the second ejector 6 and reverse valve 16, and rises in the liquid stored in the dissolution tank 1. During this time, ozone in the gas dissolves into water, producing ozone-dissolved water. On the other hand, the undissolved portion of the osinated gas remains in the upper part of the dissolution tank 1, but it is sent to the second ejector 6 via the ozone circulation pipe 11, and is taken into the pressurized water supply flowing through the water supply pipe 9 again. The ozone flows into the dissolution tank 1 via the upper valve 16, and the ozone therein is circulated so as to be incorporated into the solution. Furthermore, the dissolving tank 1 is provided with a solenoid valve 15 that branches from the discharge pipe 13 on the upstream side of the discharge valve 12 of the discharge pipe 13 and immediately after the branch, and the terminal end is connected to the water supply pipe 9 upstream of the water supply pump 2. A reflux pipe 14 connected to the side is provided. Therefore, when the water supply pump 2 is driven with the discharge valve 13 closed or slightly open and the solenoid valve 15 open, the ion-dissolved water in the dissolution tank 1 returns to the water supply pipe 9 via the circulation pipe 14 and further. The water supply pump 21 is arranged to generate a circulation flow that returns to the melting tank 1.

又溶解槽1#こは、内部に貯留されているオゾン溶解水
の水位を検出し、設定水位との増減がある場合電気信号
を出力するレベルスイッチ7が配備され、さらに溶解槽
1内に滞留する未溶解のオゾン化ガスの圧力を検知し、
それが設定圧より高くなったら電気信号を出力する圧力
スイッチ19と。
In addition, dissolution tank 1 # is equipped with a level switch 7 that detects the water level of ozone dissolved water stored inside and outputs an electric signal if there is an increase or decrease from the set water level. detects the pressure of undissolved ozonized gas,
and a pressure switch 19 that outputs an electric signal when the pressure becomes higher than the set pressure.

該スイッチ19の電気信号によって開閉が制御される電
磁弁20とオゾン接触分解器21とが介装されている放
出管22とが接続されていて、溶解槽l内の滞留イオン
化ガスの圧が設定圧より高くなったら該ガス中のオゾン
を分解し無害化して大気中へ放散させるようになってい
る。
A solenoid valve 20 whose opening/closing is controlled by an electric signal from the switch 19 is connected to a discharge pipe 22 in which an ozone catalytic decomposer 21 is installed, and the pressure of the ionized gas retained in the dissolution tank l is set. When the pressure becomes higher than that, the ozone in the gas is decomposed, rendered harmless, and released into the atmosphere.

上記のように構成されたオゾン溶解水製造装置は、図示
しない供給栓の開閉に応動して排出弁12及び電磁弁8
の開閉と、駆動モータ3及びオゾン発生装置4の駆動と
が制御されるようになっており、その制御系は破線で示
されている。すなわち図示しない供給栓が開放されると
、駆動モータ3及びオゾン発生装置4が駆動され、それ
とともに排水弁12及び電磁弁8が開放される。したが
って溶解槽1内に貯留されているオゾン溶解水の送出が
始まると同時に、給水ポンプ2が駆動され給水管9内に
加圧給水が流れ第1エゼクタ5及び第2エゼクタ6を通
流するので、該給水中にオゾン化ガスを吸引混入しオゾ
ン溶解水の製造が始まり。
The ozone-dissolved water production apparatus configured as described above operates by the discharge valve 12 and the solenoid valve 8 in response to the opening and closing of the supply valve (not shown).
The opening/closing of the ozone generator and the driving of the drive motor 3 and ozone generator 4 are controlled, and the control system is shown by broken lines. That is, when the supply tap (not shown) is opened, the drive motor 3 and the ozone generator 4 are driven, and at the same time, the drain valve 12 and the solenoid valve 8 are opened. Therefore, at the same time as the delivery of the ozone dissolved water stored in the dissolution tank 1 starts, the water supply pump 2 is driven and pressurized water flows into the water supply pipe 9 and passes through the first ejector 5 and the second ejector 6. The production of ozone-dissolved water begins by sucking and mixing ozonized gas into the water supply.

溶解槽l内でもオゾンの溶解が進められかつオゾン溶解
水が貯留されていくのである。その際溶解槽1内の水位
が設定水位より下がるので、それをレベルスイッチ7が
検知し電気信号を出力し、駆動モータ3及びオゾン発生
装置4の駆動と電磁弁8の開放を続けさせるようにする
とともに、環流管14の電磁弁15を開放させるように
働ら(。
Ozone is further dissolved in the dissolution tank 1, and ozone-dissolved water is stored. At that time, the water level in the dissolution tank 1 falls below the set water level, so the level switch 7 detects this and outputs an electric signal to continue driving the drive motor 3 and ozone generator 4 and opening the solenoid valve 8. At the same time, it works to open the solenoid valve 15 of the circulation pipe 14 (.

一方供給栓が閉基されオゾン溶解水の供給が止むと、そ
れに伴ない駆動モータ3及びオゾン発生装[4の停止と
排出弁12及び!@弁8の閉塞が指示されるが、レベル
スイッチ7からの電気信号が生きているためオゾン溶解
水の供給が止まり溶解槽1内の水位が上昇し設定水位に
達するまでの開駆動モータ3及びオゾン発生装置4の駆
動と電磁弁8及び15の開放は続けられ、槽1内の水位
が設定水位に達して始めてすべてが停止され閉塞するよ
うに制御されるのである。この場合長時間オゾン溶解水
の送出がないと、オゾン溶解水のオゾン濃度が漸時減衰
していく問題は避けられないが。
On the other hand, when the supply valve is closed and the supply of ozone-dissolved water is stopped, the drive motor 3 and the ozone generator [4] are stopped, and the discharge valve 12 and... @ Valve 8 is instructed to close, but since the electric signal from the level switch 7 is still active, the supply of ozone dissolved water is stopped and the water level in the dissolving tank 1 rises until the opening drive motor 3 and The operation of the ozone generator 4 and the opening of the electromagnetic valves 8 and 15 are continued, and control is such that everything is stopped and closed only when the water level in the tank 1 reaches the set water level. In this case, if ozone-dissolved water is not sent out for a long time, the problem that the ozone concentration of the ozone-dissolved water gradually decreases cannot be avoided.

使用頻度が高く供給栓の開閉が頻譬に行なわれるような
ケースには好適なオゾン溶解水製造装置である。
This ozone-dissolved water production device is suitable for cases where the supply valve is frequently opened and closed due to frequent use.

第2図に示すオゾン溶解水製造装置は、既述の装置に駆
動モータ3及びオゾン発生装置4の駆動と停止ならびに
電磁fP8及び15の開と閉を周期的に繰返すように、
一定時間毎1こ電気信号を出力するタイマ17を付加す
るととも1こ、環流管14の電磁弁15の開閉制御をレ
ベルスイッチ7からの電気信号によらずタイマ17の出
力信号で行なうように構成したものである。すなわちイ
オン溶解水の送出に応動する装置各部の働らきは既述の
通りであるが、該溶解水の供給が停止し、装置が長時間
休止している間でも間欠的に溶解槽1内のイオン溶解水
を環流管14を介して循環させるようにしである点が既
述のオゾン溶解水製a装置と異るところであり、オゾン
溶解水のオゾン濃度の減衰を防止し該濃度のバラツキが
ないオゾン溶解水を供給することができるメリットがあ
る。
The ozone-dissolved water production apparatus shown in FIG. 2 includes the above-described apparatus so as to periodically repeat driving and stopping of the drive motor 3 and ozone generator 4 and opening and closing of the electromagnetic fPs 8 and 15.
By adding a timer 17 that outputs one electric signal every fixed period of time, the opening and closing control of the solenoid valve 15 of the circulation pipe 14 is controlled by the output signal of the timer 17 without depending on the electric signal from the level switch 7. This is what I did. In other words, the functions of each part of the device that responds to the delivery of ion-dissolved water are as described above, but even when the supply of ion-dissolved water is stopped and the device is stopped for a long time, the contents of the dissolution tank 1 are intermittently This device differs from the ozone-dissolved water device A in that the ion-dissolved water is circulated through the reflux pipe 14, which prevents the ozone concentration of the ozone-dissolved water from attenuating and eliminates variations in the concentration. It has the advantage of being able to supply ozone-dissolved water.

第3図に示すオゾン溶解水製造装置は、第1図のイオン
溶解水製造装置の溶解[1に、該$1内に滞留している
オゾン化ガスのオゾン濃度を検出し、それが設定濃度よ
り低下している間だけ駆動モータ3及びオゾン発生装置
4を駆動し電磁弁8及び15を開放させる電気信号を出
力するオゾン濃度検出器18を付設するとともに、環流
管14の電磁弁15の開閉制御をレベルスイッチ7から
の電気信号によらずオゾン濃度検出器18の出力信号に
よって行なうように構成したものである。
The ozone-dissolved water manufacturing device shown in FIG. An ozone concentration detector 18 is attached that outputs an electric signal that drives the drive motor 3 and the ozone generator 4 and opens the solenoid valves 8 and 15 only while the ozone concentration is lower, and also opens and closes the solenoid valve 15 of the circulation pipe 14. The control is not based on the electric signal from the level switch 7 but on the output signal of the ozone concentration detector 18.

すなわちイオン溶解水の送出に応動する装置各部の働ら
きは第1図の説明の通りであるが、溶解槽1内の滞留オ
ゾン化ガス中のオゾン濃度に感応して、溶解槽1内のイ
オン溶解水を循環させ同時に新しいオゾン化ガスを送り
込み、液中のオゾン濃度を一定に維持するようにした点
が既述の実施例とは異るところである。したがって液中
のオゾン濃度が低下している間だけ駆動モータ3及びオ
ゾン発生装wL4を駆動させ、槽1内のオゾン溶解水を
循環させオゾン化ガスを供給するように構成されるので
、エネルギの浪費がなくかつ均一なオゾン濃度のイオン
溶解水をいつでも供給できるきわめて経済性の高いイオ
ン溶解水製造装置となるのである。
In other words, the functions of the various parts of the device that respond to the delivery of ion-dissolved water are as explained in FIG. This differs from the previously described embodiments in that dissolved water is circulated and at the same time new ozonized gas is fed in to maintain a constant ozone concentration in the liquid. Therefore, the drive motor 3 and the ozone generator wL4 are driven only while the ozone concentration in the liquid is decreasing, and the ozone-dissolved water in the tank 1 is circulated to supply ozonized gas. This results in an extremely economical ion-dissolved water production device that can supply ion-dissolved water with uniform ozone concentration at any time without waste.

〔発明・の効果〕〔Effect of the invention〕

以上説明したことから明らかなように、本発明によれば
イオン溶解水製造装置を、排水弁を備えび逆止弁を直列
に介装し、給水ポンプの駆動によりオゾン発生装置から
のオゾン化ガスをifエゼクタを介して給水中に混入オ
ゾンを溶解させ、さらに溶解槽に滞留する未溶解のオゾ
ン化ガスを第2エゼクタへ送り給水中へ混入させるとい
った具合にオゾンの溶解する機会を2段階にするととも
に、排出管と給水賃とが連通ずる環流管を設け、貯留槽
内に貯留されているオゾン溶解水が環流管及び給水管を
介して溶解槽へ還流する循環流を生成せしめ新しいオゾ
ン化ガスを送入するよう番こ構成しであるので、オゾン
化ガス中のオゾンの水への溶解が良好に行なわれオゾン
濃度の高いオゾン溶解水を容易に製造することができ、
さらに未溶解のオゾン化ガスはオゾン接触分解器を介し
て無害化して大気中へ放散する手段を購しであるので環
境へのオゾンの害を皆無とすることができるようになっ
ているまた。レベルスイッチ、圧力スイッチ、タイマ及
びオゾン濃度検出器を配備することにより、オゾン溶解
水のオゾン濃度の減衰を防止することが自動的に行なわ
れるようにすることも出来るので、装置全体のバランス
を考えてコンパクトに設計することにより、オゾン溶解
水装置を、溶解オゾン濃度がほぼ一定で洗浄力の強いオ
ゾンのである。
As is clear from the above explanation, according to the present invention, the ion-dissolved water production device is equipped with a drain valve and a check valve interposed in series, and the ozonized gas from the ozone generator is driven by the water supply pump. The ozone is dissolved in the water supply through the ejector, and the undissolved ozonized gas remaining in the dissolution tank is sent to the second ejector and mixed into the water supply. At the same time, a circulation pipe is installed in which the discharge pipe and the water supply are connected, and a circulation flow is created in which the ozone-dissolved water stored in the storage tank returns to the dissolution tank via the circulation pipe and the water supply pipe, resulting in new ozonization. Since the filter is configured to feed gas, the ozone in the ozonized gas is well dissolved in water, and ozone-dissolved water with a high ozone concentration can be easily produced.
Furthermore, undissolved ozonized gas is rendered harmless through an ozone catalytic decomposer and released into the atmosphere, thereby completely eliminating the harm caused by ozone to the environment. By installing a level switch, pressure switch, timer, and ozone concentration detector, it is possible to automatically prevent the ozone concentration of the ozone dissolved water from decreasing, so consider the overall balance of the device. With its compact design, the ozone-dissolved water device uses ozone with almost constant dissolved ozone concentration and strong cleaning power.

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

第1図は実施例のオゾン溶解水製造装置の概略構成図で
、第2図及び第3図はそれぞれ他の実施例のイオン溶解
水製造装置の概略構成図であり。 第4図ないし第6図はそれぞれ従来のイオン溶解水製造
装置の概略を示す構成図である。 1:#解槽、2:給水ポンプ、3:給水ポンプ駆動用電
動機(駆動モータ)、4ニオシン発生装置、5:第1エ
ゼクタ、6:第2エゼクタ、7:レベルスイッチ、8,
15.20:電磁弁、9:給水管、10ニオシン送出管
、11ニオシン環流管、12:排出弁、13:排出管、
14:環流管。 17:タイマ、18ニオシン濃度検出器、19:圧力ス
イッチ、21ニオシン接触分解器、22:放出管。 笛4(2) 笥5(2)
FIG. 1 is a schematic diagram of an ozone-dissolved water production apparatus according to an embodiment, and FIGS. 2 and 3 are schematic diagrams of ion-dissolved water production apparatuses according to other embodiments. FIGS. 4 to 6 are block diagrams schematically showing conventional ion-dissolved water production apparatuses. 1: #Tank disassembly, 2: Water supply pump, 3: Electric motor for driving the water supply pump (drive motor), 4 Niosin generator, 5: First ejector, 6: Second ejector, 7: Level switch, 8,
15.20: Solenoid valve, 9: Water supply pipe, 10 Niosine delivery pipe, 11 Niosine reflux pipe, 12: Discharge valve, 13: Discharge pipe,
14: Reflux tube. 17: timer, 18 niosine concentration detector, 19: pressure switch, 21 niosine catalytic decomposer, 22: discharge pipe. Flute 4 (2) Porch 5 (2)

Claims (1)

【特許請求の範囲】 1)オゾン発生装置と、オゾンを溶解し貯留する溶解槽
と、給水ポンプ、第1エゼクタ、第2エゼクタ及び逆止
弁を直列に介装し前記溶解槽に接続される給水管と、排
出弁を備え前記溶解槽内のオゾン溶解水を送出する排出
管と、前記溶解槽内に滞留するオゾン化ガスを抽出し前
記第2エゼクタへ送流するオゾン環流管と、前記滞留オ
ゾン化ガス圧力が設定値を超過したら電気信号を出力す
る圧力スイッチと、該圧力スイッチの出力信号で開閉が
制御される電磁弁とオゾン接触分解器とを介装している
放出管と、前記溶解槽内の水位が設定値からはずれたら
電気信号を出力するレベルスイッチとを配備するととも
に、前記オゾン発生装置からのオゾン化ガスを前記第1
エゼクタへ送流する電磁弁が配されたオゾン送出管と、
前記排出弁の上流で前記排出管から分岐し前記給水ポン
プの上流側で前記給水管に接続される電磁弁を備えた環
流管とから形成され、前記溶解槽からのオゾン溶解水の
送出に応動して前記排出弁及びオゾン送出管の電磁弁の
開閉と、前記給水ポンプの駆動モータならびにオゾン発
生装置の駆動とを制御し、さらに前記レベルスイッチの
出力信号によって前記環流管及びオゾン送出管の電磁弁
の開閉と、前記給水ポンプの駆動モータならびにオゾン
発生装置の駆動とが制御されるように構成したことを特
徴とするオゾン溶解水製造装置。 2)特許請求の範囲第1項記載の製造装置において、該
製造装置にオゾン送出管及び環流管の電磁弁の開又は閉
と、給水ポンプの駆動モータ及びオゾン発生装置の駆動
又は停止を、周期的に繰返すように電気信号を出力する
タイマを付加し、所定時間毎に給水ポンプを駆動し溶解
槽内のオゾン溶解水が環流管及び給水管を介して循環す
るように構成したことを特徴とするオゾン溶解水製造装
置。 3)特許請求の範囲第1項に記載のオゾン溶解水製造装
置において、溶解槽に、該槽内に滞留しているオゾン化
ガスのオゾン濃度を検出し設定値より低いとき電気信号
を出力するオゾン濃度検出器を付設し、該検出器の出力
によってオゾン送出管及び環流管の電磁弁の開閉と、給
水ポンプの駆動モータならびにオゾン発生装置の駆動と
を制御させ、溶解槽内のイオン溶解水が環流管及び給水
管とを介して循環するように構成したことを特徴とする
イオン溶解製造装置。
[Claims] 1) An ozone generator, a dissolution tank for dissolving and storing ozone, a water supply pump, a first ejector, a second ejector, and a check valve are interposed in series and connected to the dissolution tank. a water supply pipe, a discharge pipe that is equipped with a discharge valve and sends out the ozone-dissolved water in the dissolution tank, an ozone reflux pipe that extracts the ozonized gas remaining in the dissolution tank and sends it to the second ejector; a pressure switch that outputs an electric signal when the pressure of the accumulated ozonized gas exceeds a set value; a discharge pipe that is interposed with an ozone catalytic decomposer and a solenoid valve whose opening and closing are controlled by the output signal of the pressure switch; A level switch is provided that outputs an electric signal when the water level in the dissolution tank deviates from a set value, and the ozonized gas from the ozone generator is supplied to the first
An ozone delivery pipe equipped with a solenoid valve that sends water to the ejector,
a reflux pipe branched from the discharge pipe upstream of the discharge valve and equipped with an electromagnetic valve connected to the water supply pipe upstream of the water supply pump, and responsive to the delivery of ozone dissolved water from the dissolution tank. controls the opening and closing of the discharge valve and the solenoid valve of the ozone delivery pipe, and the driving of the drive motor of the water supply pump and the ozone generator, and further controls the electromagnetic valve of the circulation pipe and the ozone delivery pipe by the output signal of the level switch. An ozone-dissolved water production device characterized in that the opening and closing of a valve, the drive motor of the water supply pump, and the drive of the ozone generator are controlled. 2) In the manufacturing apparatus according to claim 1, the manufacturing apparatus is configured to periodically open or close the solenoid valves of the ozone delivery pipe and the return pipe, and to drive or stop the drive motor of the water pump and the ozone generator. A timer is added to output an electric signal repeatedly, and the water supply pump is driven at predetermined intervals so that the ozone dissolved water in the dissolution tank is circulated through the circulation pipe and the water supply pipe. Ozone-dissolved water production equipment. 3) In the ozone-dissolved water production apparatus according to claim 1, the ozone concentration of the ozonized gas retained in the dissolution tank is detected and an electric signal is output when the ozone concentration is lower than a set value. An ozone concentration detector is attached, and the output of the detector controls the opening and closing of the solenoid valves of the ozone delivery pipe and the return pipe, the drive motor of the water supply pump, and the drive of the ozone generator. An ion dissolution production device characterized in that the ion dissolution manufacturing device is configured such that the water is circulated through a reflux pipe and a water supply pipe.
JP25121286A 1986-10-22 1986-10-22 Apparatus for producing ozone dissolved water Pending JPS63104697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25121286A JPS63104697A (en) 1986-10-22 1986-10-22 Apparatus for producing ozone dissolved water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25121286A JPS63104697A (en) 1986-10-22 1986-10-22 Apparatus for producing ozone dissolved water

Publications (1)

Publication Number Publication Date
JPS63104697A true JPS63104697A (en) 1988-05-10

Family

ID=17219365

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25121286A Pending JPS63104697A (en) 1986-10-22 1986-10-22 Apparatus for producing ozone dissolved water

Country Status (1)

Country Link
JP (1) JPS63104697A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0372993A (en) * 1989-08-10 1991-03-28 Ishikawajima Harima Heavy Ind Co Ltd Ozone manufacturing device
JPH05245354A (en) * 1992-03-04 1993-09-24 Yoshihiko Terasawa Air-water ejector
JP3033969U (en) * 1996-07-25 1997-02-07 東海プラントエンジニアリング株式会社 Bubble tower gas-liquid contactor
US6568900B2 (en) 1999-02-01 2003-05-27 Fantom Technologies Inc. Pressure swing contactor for the treatment of a liquid with a gas
KR100687704B1 (en) 2005-07-22 2007-03-02 에스아이비(주) An Ozone transfusion device and method for water treatment
US8002247B2 (en) * 2008-08-22 2011-08-23 Air Products And Chemicals, Inc. Cross purge valve and container assembly
JP2018153727A (en) * 2017-03-15 2018-10-04 住友精密工業株式会社 Ozone water supply system
JP2022179290A (en) * 2021-05-20 2022-12-02 ピュリテク カンパニー リミテッド System for dissolving gas

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5142352A (en) * 1974-10-08 1976-04-09 Akyoshi Sakurai OZONOHATSUSEISURUSHIGAISENSATSUKINTOOMOCHIITENO EKITAIJOKAMUKINSOCHI
JPS5310390A (en) * 1976-07-16 1978-01-30 Mitsubishi Electric Corp Treating apparatus with ozone
JPS6023039U (en) * 1983-07-22 1985-02-16 興亜硝子株式会社 medicine bottle

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5142352A (en) * 1974-10-08 1976-04-09 Akyoshi Sakurai OZONOHATSUSEISURUSHIGAISENSATSUKINTOOMOCHIITENO EKITAIJOKAMUKINSOCHI
JPS5310390A (en) * 1976-07-16 1978-01-30 Mitsubishi Electric Corp Treating apparatus with ozone
JPS6023039U (en) * 1983-07-22 1985-02-16 興亜硝子株式会社 medicine bottle

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0372993A (en) * 1989-08-10 1991-03-28 Ishikawajima Harima Heavy Ind Co Ltd Ozone manufacturing device
JPH05245354A (en) * 1992-03-04 1993-09-24 Yoshihiko Terasawa Air-water ejector
JP3033969U (en) * 1996-07-25 1997-02-07 東海プラントエンジニアリング株式会社 Bubble tower gas-liquid contactor
US6568900B2 (en) 1999-02-01 2003-05-27 Fantom Technologies Inc. Pressure swing contactor for the treatment of a liquid with a gas
KR100687704B1 (en) 2005-07-22 2007-03-02 에스아이비(주) An Ozone transfusion device and method for water treatment
US8002247B2 (en) * 2008-08-22 2011-08-23 Air Products And Chemicals, Inc. Cross purge valve and container assembly
JP2018153727A (en) * 2017-03-15 2018-10-04 住友精密工業株式会社 Ozone water supply system
JP2022179290A (en) * 2021-05-20 2022-12-02 ピュリテク カンパニー リミテッド System for dissolving gas

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