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JPH0655311B2 - Ozone water production system - Google Patents
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JPH0655311B2 - Ozone water production system - Google Patents

Ozone water production system

Info

Publication number
JPH0655311B2
JPH0655311B2 JP3040487A JP4048791A JPH0655311B2 JP H0655311 B2 JPH0655311 B2 JP H0655311B2 JP 3040487 A JP3040487 A JP 3040487A JP 4048791 A JP4048791 A JP 4048791A JP H0655311 B2 JPH0655311 B2 JP H0655311B2
Authority
JP
Japan
Prior art keywords
ozone
water
reaction tube
ozone water
ozone gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP3040487A
Other languages
Japanese (ja)
Other versions
JPH04260496A (en
Inventor
武仁 大谷
仁 高橋
秋夫 大野
孝文 松永
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP3040487A priority Critical patent/JPH0655311B2/en
Publication of JPH04260496A publication Critical patent/JPH04260496A/en
Publication of JPH0655311B2 publication Critical patent/JPH0655311B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明はオゾン殺菌、オゾン漂
白、脱臭等に使用されるオゾン水を供給するためのオゾ
ン水製造システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ozone water production system for supplying ozone water used for ozone sterilization, ozone bleaching, deodorization and the like.

【0002】[0002]

【従来の技術】電解法によるオゾンガス発生器を用いて
オゾン水を得るオゾン水製造装置のオゾン水濃度を調節
する場合、オゾンガス発生器の電流値を調節して行って
いた。
2. Description of the Related Art When adjusting the ozone water concentration of an ozone water producing apparatus for obtaining ozone water using an ozone gas generator by an electrolysis method, the current value of the ozone gas generator is adjusted.

【0003】この方法では、電流値を調節してからオゾ
ンガスの発生量が安定するまで数十分時間がかかる。ま
た、オゾン水を得る方法としては一般的にオゾンガスを
水中に吹き込み、気泡を分散させることからなる散気板
型オゾン接触塔を使用するが、この方法では、オゾンガ
スの発生量に対してオゾン水濃度は1つしか得られな
い。
In this method, it takes several tens of minutes until the amount of ozone gas generated is stabilized after the current value is adjusted. As a method for obtaining ozone water, a diffuser plate type ozone contact tower consisting of blowing ozone gas into water and dispersing bubbles is generally used. Only one concentration can be obtained.

【0004】[0004]

【発明が解決しようとする課題】前述の方法は、操作は
容易であるが、必要なオゾン水を得るためにはオゾンガ
スの発生が安定するまでの時間約30分〜1時間とその
安定したオゾンガスを用い、必要なオゾン水濃度に達す
るまでの時間が約10〜20分で、非常に時間がかか
る。
The above-mentioned method is easy to operate, but in order to obtain the necessary ozone water, the time until the generation of ozone gas stabilizes is about 30 minutes to 1 hour and the stable ozone gas. It takes about 10 to 20 minutes to reach the required ozone water concentration, and it takes a very long time.

【0005】本発明は上記課題を解決するためになされ
たもので、その目的は特に純水を電気分解して得られた
オゾンガスを反応筒内に放出充満させ、噴霧水を放出し
てオゾンガスと接触溶解させて発生部を調節せずに異な
った濃度のオゾン水をスイッチのオン、オフで蛇口から
放出することのできるオゾン水製造システムを提供する
ことにある。
The present invention has been made in order to solve the above-mentioned problems, and its purpose is to discharge and fill the reaction tube with ozone gas obtained by electrolyzing pure water, and to discharge the spray water to generate ozone gas. It is an object of the present invention to provide an ozone water production system capable of discharging ozone water of different concentrations from a faucet by contact-dissolving without adjusting the generation part and turning the switch on and off.

【0006】[0006]

【課題を解決するための手段】即ち、本発明は反応筒
(5)と、反応筒(5')に設けられた噴霧ノズル(4、4')と、
水を電気分解してオゾンガスを得るためのオゾナイザ(1
1)と、オゾナイザからのオゾンガスを前記反応筒内に放
出する散気具(2、2')と、反応筒の下部に接続されたオ
ゾン水貯留槽(10、10')と、得られたオゾン水を放出す
る液体ポンプ(6、6')を備えてなる反応筒を2個以上直
列に接続し、前記貯留槽間をオゾン水が循環できる流路
(7)を備えてなるオゾン水製造システムに係る。
That is, the present invention is a reaction tube.
(5), and a spray nozzle (4, 4 ') provided in the reaction tube (5'),
Ozonizer for electrolyzing water to obtain ozone gas (1
1), a diffuser for discharging ozone gas from the ozonizer into the reaction tube (2, 2 '), and an ozone water storage tank (10, 10') connected to the lower part of the reaction tube, A flow path in which two or more reaction tubes equipped with liquid pumps (6, 6 ') that discharge ozone water are connected in series to allow ozone water to circulate between the storage tanks.
The present invention relates to an ozone water production system including (7).

【0007】また、本発明のオゾン水製造システムは最
低2個の反応筒内に空気を送り込むためのエアーポンプ
(22)と、前記反応筒の上部に接続し、オゾンガスを分解
無害化するオゾンキラー(20)とを備え、前記反応筒内に
残留した残余オゾンガスを前記エアーポンプからの空気
によって前記オゾンキラーに送り、オゾンガスを分解無
害化後、系外へ放出するような構成とすることができ
る。
The ozone water production system of the present invention is an air pump for feeding air into at least two reaction tubes.
(22), and an ozone killer (20) connected to the upper part of the reaction tube and decomposing and detoxifying ozone gas, the residual ozone gas remaining in the reaction tube is supplied to the ozone killer by air from the air pump. The ozone gas may be sent, decomposed and detoxified, and then discharged to the outside of the system.

【0008】[0008]

【作用】本発明によるオゾン水製造システムにおいて
は、オゾンガスを充満させた反応筒(5、5')に多量の噴
霧水を一液用ノズル(4、4')から供給するため、オゾン
ガスと水との接触面積が大きくとれ、オゾン水生成効率
が増大する。
In the ozone water production system according to the present invention, since a large amount of spray water is supplied from the one-liquid nozzle (4, 4 ') to the reaction tube (5, 5') filled with ozone gas, ozone gas and water A large contact area with the ozone water can be obtained, and the ozone water generation efficiency is increased.

【0009】また、オゾン水の流れが直列になるように
最低2個のオゾン反応筒を接続しているので、給水され
た水は最初の反応筒の一液用ノズル(4')でオゾンガスと
接触した上、次の反応筒の一液用ノズル(4)で再びオゾ
ンガスと接触する。
Also, since at least two ozone reaction tubes are connected so that the flow of ozone water is in series, the supplied water is converted into ozone gas at the one-liquid nozzle (4 ') of the first reaction tube. After coming into contact with the ozone gas, the one-liquid nozzle (4) for the next reaction tube again comes into contact with ozone gas.

【0010】一方、オゾンガスは接続された2個以上の
反応筒の中でオゾン水の流れ方向の最後尾の反応筒(5)
に入り、オゾン水と接触する。この反応筒で水と接触し
たオゾンガスのうち、未溶解の残存オゾンガスはこの反
応筒(5)に接続されている排オゾン通路(1')を通り、手
前の反応筒(5')に導かれ、水またはオゾン水と接触する
ので1つの反応筒よりガスと水の接触の回数が多くな
る。従って、1つの反応筒より高い濃度のオゾン水が得
られる。
On the other hand, ozone gas is the last reaction tube (5) in the flow direction of ozone water among the two or more reaction tubes connected.
Enters into contact with ozone water. Of the ozone gas that has come into contact with water in this reaction tube, the undissolved residual ozone gas passes through the exhaust ozone passage (1 ') connected to this reaction tube (5) and is guided to the front reaction tube (5'). Since it comes into contact with water or ozone water, the number of times of contact between gas and water is larger than in one reaction tube. Therefore, ozone water having a higher concentration than one reaction cylinder can be obtained.

【0011】更に、反応筒の下部にある貯留槽のオゾン
水を流路(7)−貯留槽B(10')−ポンプ(6')−放出路(14)
−噴霧ノズル(4)−貯留槽A(10)と再循環させることに
よって、更に高い濃度のオゾン水を間欠的に得ることが
できる。従って、本システムによれば少なくとも3種類
以上の濃度のオゾン水が弁の切り換えにより得られる。
すなわち、反応筒1個で得られるオゾン水濃度、2個以
上直列に用いた時のオゾン水濃度及び間欠に水を1個ま
たは2個以上の反応筒間で再循環させたときのオゾン水
濃度である。
Further, the ozone water in the storage tank at the lower part of the reaction tube is flow path (7) -storage tank B (10 ')-pump (6')-release path (14).
-By recirculating the spray nozzle (4) -reservoir A (10), ozone water having a higher concentration can be intermittently obtained. Therefore, according to the present system, ozone water having at least three kinds of concentrations can be obtained by switching the valve.
That is, the ozone water concentration obtained by one reaction tube, the ozone water concentration when two or more reaction tubes are used in series, and the ozone water concentration when water is intermittently recirculated between one or two reaction tubes. Is.

【0012】[0012]

【実施例】図1に本発明のオゾン水製造システムの1実
施態様を示す。図1にはオゾンガスをオゾン水に変換す
るための反応筒A(5)と反応筒B(5')が設けられてお
り、この反応筒A(5)内にはオゾナイザ(11)からのオゾ
ンガスをガス通路A(1)及び逆止弁(23)を介して放出す
る散気具(2)が設けられ、その上部位置には、水を反応
筒A(5)内に噴霧するための一液用ノズル(4)を取り付け
た噴霧ノズル取付パイプ(3)が設けられている。同様
に、反応筒B(5')内には、反応筒A(5)で未溶解のオゾ
ンガスを反応筒A(5)の上部に取り付けられた排オゾン
通路A(1')及び排オゾン通路電磁弁(19)を介して放出す
る散気具(2')が設けられ、その上部位置には水を反応筒
B(5')内に噴霧するための一液用ノズル(4')を取り付け
た噴霧ノズル取付パイプ(3')が設けられると共にオゾン
水製造にて余ったオゾンガスを反応筒A(5)及び反応筒
B(5')外に放出するため逆止弁(24)を介した一端にエア
ーポンプ(22)が設けられた空気通路(21)が設けられてお
り、更に、反応筒A(5)及びB(5')の下部には、オゾン
水あるいは水をためておく貯留槽A(10)及びB(10')が
設けられており、貯留槽B(10')には反応筒B(5')で製
造したオゾン水あるいは水を反応筒A(5)に放出するた
めの放出路(14)が電磁弁(16)を介して設けてあり、貯留
槽A(10)には、反応筒A(5)で製造したオゾン水あるい
は水を放出するための放水路(25)が電磁弁(26)を介して
設けてある。また、貯留槽A(10)及びB(10')には水位
計(8)、(9)及び(8')、(9')がそれぞれ設けてある。これ
は貯留槽内の水位を一定にすることによりオゾンガスの
接触面積を一定とすることができ、更に、オゾン水濃度
も一定にできるためである。更に、貯留槽A(10)とB(1
0')には、電磁弁(17)を介して接続している流路(7)が設
けてある。
EXAMPLE FIG. 1 shows one embodiment of the ozone water production system of the present invention. In FIG. 1, a reaction tube A (5) and a reaction tube B (5 ') for converting ozone gas into ozone water are provided, and the ozone gas from the ozonizer (11) is provided in the reaction tube A (5). An air diffuser (2) for discharging the gas through the gas passage A (1) and the check valve (23) is provided, and at the upper position thereof, there is provided one for spraying water into the reaction tube A (5). A spray nozzle mounting pipe (3) to which a liquid nozzle (4) is mounted is provided. Similarly, in the reaction tube B (5 '), the ozone gas undissolved in the reaction tube A (5) is attached to the upper part of the reaction tube A (5), and the exhaust ozone passage A (1') and the exhaust ozone passage An air diffuser (2 ') for discharging via a solenoid valve (19) is provided, and a one-liquid nozzle (4') for spraying water into the reaction tube B (5 ') is provided at the upper position thereof. The attached spray nozzle mounting pipe (3 ') is provided and a check valve (24) is provided to discharge the ozone gas remaining in the ozone water production to the outside of the reaction cylinder A (5) and the reaction cylinder B (5'). An air passage (21) provided with an air pump (22) is provided at one end, and ozone water or water is stored under the reaction tubes A (5) and B (5 '). Storage tanks A (10) and B (10 ') are provided, and the storage tank B (10') releases ozone water or water produced in the reaction tube B (5 ') to the reaction tube A (5). A discharge passage (14) for controlling the The vessel A (10), spillway for discharging the ozone water or water produced by the reaction column A (5) (25) is provided via a solenoid valve (26). The storage tanks A (10) and B (10 ') are provided with water level gauges (8), (9) and (8'), (9 '), respectively. This is because the contact area of ozone gas can be made constant by making the water level in the storage tank constant, and the ozone water concentration can also be made constant. Furthermore, storage tanks A (10) and B (1
The flow path (7) connected to the solenoid valve (17) is provided in 0 ').

【0013】まず、3種類の濃度のうち一番低い濃度を
製造する場合、オゾナイザ(11)から発生したオゾンガス
が反応筒A(5)内の散気具(2)より放出され、反応筒A
(5)内に導入される。そこに一液用ノズル(4)より噴霧さ
れる水と接触溶解したオゾン水が貯留槽A(10)内に溜ま
り、オゾン水の水位が一定になると貯留槽A(10)内の水
位計(9)及び(8)からの信号によってオゾン水が電磁弁(2
6)を介してオゾン放出路(25)よりポンプ(6)によって放
出される。
First, in the case of producing the lowest concentration of the three kinds of concentrations, the ozone gas generated from the ozonizer (11) is discharged from the air diffuser (2) in the reaction cylinder A (5) and the reaction cylinder A
Introduced in (5). Ozone water that has been contact-dissolved with water sprayed from the one-liquid nozzle (4) there accumulates in the storage tank A (10), and when the water level of the ozone water becomes constant, a water level gauge ( Ozone water is sent to the solenoid valve (2
It is discharged by the pump (6) from the ozone discharge path (25) via 6).

【0014】この場合、給水しながら放出することによ
って連続的にオゾン水を得ることができる。この場合、
給水路(13)−電磁弁(15)−噴霧ノズル取付パイプ(3)−
一液用ノズル(4)の経路で流れ、排オゾンガスは排オゾ
ンガス通路B(12)−電磁弁(18)−オゾンキラー(20)の経
路で排出され、その他の電磁弁(15'、16、17、18'、19)
は閉じられている。
In this case, ozone water can be continuously obtained by discharging while supplying water. in this case,
Water supply channel (13) -Solenoid valve (15) -Spray nozzle mounting pipe (3)-
The exhaust ozone gas flows through the path of the one-liquid nozzle (4) and is discharged through the path of the exhaust ozone gas passage B (12) -solenoid valve (18) -ozone killer (20), and the other solenoid valves (15 ', 16, (17, 18 ', 19)
Is closed.

【0015】次に、前記オゾン水よりも高い濃度のオゾ
ン水を製造する場合、排オゾンガス通路A(1')に設けて
ある電磁弁(19)を開けることによりオゾナイザ(11)で発
生したオゾンガスは一端に散気具(2)を設けた排オゾン
ガス通路A(1)を通って反応筒A(5)に導入され、一端に
散気具(2')を設けた排オゾンガス通路A(1')を通って反
応筒B(5')内にも導入される。一液用ノズル(4')よりそ
こへ噴霧された水はオゾンガスと接触し、オゾン水とな
って貯留槽B(10')内の水位計(9')及び(8')からの信号
によって電磁弁(16)を介して放出路(14)よりポンプ(6')
によってオゾンガスが導入してある反応筒A(5)内の一
液用ノズル(4)より噴霧水となり、オゾンガスと再び接
触し、更に高い濃度のオゾン水となり貯留槽A(10)内に
溜まり、オゾン水の水位が一定になると貯留槽A(10)内
の水位計(9)及び(8)からの信号によってオゾン水が電磁
弁(26)を介してオゾン放出路(25)よりポンプ(6)によっ
て放出される。この場合、給水しながら放出することに
よって連続的にオゾン水を得ることができる。この場
合、給水は電磁弁(15')−給水路B(13')−噴霧ノズル取
付パイプ(3')−一液用ノズル(4')−貯留槽B(10')−ポ
ンプ(6')−放出路(14)−電磁弁(16)−噴霧ノズル取付パ
イプ(3)−一液用ノズル(4)−貯留槽A(10)−ポンプ(6)
−放出路(25)−電磁弁(26)の経路で流れ、電磁弁(18)は
閉じられている。
Next, in the case of producing ozone water having a higher concentration than the ozone water, the ozone gas generated in the ozonizer (11) is opened by opening the solenoid valve (19) provided in the exhaust ozone gas passage A (1 '). Is introduced into the reaction tube A (5) through the exhaust ozone gas passage A (1) provided with the air diffuser (2) at one end, and the exhaust ozone gas passage A (1 provided with the air diffuser (2 ') at one end. It is also introduced into the reaction tube B (5 ') through the'). The water sprayed there from the one-liquid nozzle (4 ') comes into contact with ozone gas and becomes ozone water, and signals from the water level gauges (9') and (8 ') in the storage tank B (10') are used. Pump (6 ') from discharge path (14) through solenoid valve (16)
By the one-liquid nozzle (4) in the reaction cylinder A (5) into which the ozone gas is introduced, it becomes spray water and comes in contact with the ozone gas again, and becomes ozone water of a higher concentration and collects in the storage tank A (10), When the water level of the ozone water becomes constant, the ozone water is pumped from the ozone discharge passage (25) via the solenoid valve (26) by the signals from the water level gauges (9) and (8) in the storage tank A (10). ). In this case, ozone water can be continuously obtained by discharging while supplying water. In this case, water is supplied from the solenoid valve (15 ')-water supply channel B (13')-spray nozzle mounting pipe (3 ')-single liquid nozzle (4')-reservoir B (10 ')-pump (6'). ) -Discharge path (14) -Solenoid valve (16) -Spray nozzle mounting pipe (3) -One-liquid nozzle (4) -Reservoir A (10) -Pump (6)
-The discharge path (25) -flows in the path of the solenoid valve (26), and the solenoid valve (18) is closed.

【0016】最後に、一番高い濃度のオゾン水を製造す
る場合、流路(7)に設けてある電磁弁(17)を開けること
により反応筒A(5)において、散気具(2)より導入された
ガスと一液用ノズル(4)より噴霧された水とが接触して
得られたオゾン水が、流路(7)より貯留槽B(10')に導入
される。貯留槽A(10)及び貯留槽B(10')のオゾン水の
水位が一定になると貯留槽A(10)に設けてある水位計
(9)及び(8)と貯留槽B(10')に設けてある水位計(9')及
び(8')からの信号により放出路(14)に設けてある電磁弁
(16)を介して放出路(14)よりポンプ(6')によって反応筒
A(5)内に設けてある一液用ノズル(4)よりオゾン水が噴
霧され、再びオゾンガスと接触し、更に高い濃度のオゾ
ン水を得ることができ、更に貯留槽A(10)内のオゾン水
は電動弁(17)を介した流路(7)を通って再び貯留槽B(1
0')に導入され、再び反応筒A(5)へと循環させることに
よりオゾン水濃度を上げていく。所望のオゾン水濃度に
達したら電磁弁(26)を介した放出路(25)からポンプ(6)
によって放出する。望の濃度のオゾン水になるまで循環
させるため間欠的にオゾン水を得ることができる。この
場合、給水は給水路(13)−電磁弁(15)−噴霧ノズル取付
パイプ(3)−一液用ノズル(4)−貯留槽A(10)−流路(7)
−電動弁(17)−貯留槽B(10')と流れ、所望の水量にな
ると、水位計(8、9、8'、9')の信号により電磁弁(15)を
閉じ、ポンプ(6')を運転し、貯留水を循環させる。この
とき、電磁弁(15')は閉じられている。一方、排ガスは
排オゾンガス通路B(12)−電磁弁(18)−オゾンキラー(2
0)と流れ、電磁弁(18'、19)は閉じられている。更に、
オゾン水濃度が短時間で一定になるように連続でオゾン
水を製造する場合には、給水前に貯留槽A(10)及び貯留
槽B(10')外にオゾン水を放出した後、エアーポンプ(2
2)を用いて空気を空気通路(21)、逆止弁(24)を介して反
応筒A(5)及び反応筒B(5')内に送り込み、未反応のオ
ゾンガスを排オゾンガス通路(12)を、電磁弁(18)を介し
てオゾンキラーへ排出し、反応筒A(5)及び反応筒B
(5')及び貯留槽A(10)及び貯留槽B(10')の残留オゾン
ガス量を一定に維持することができる。
Finally, in the case of producing the highest concentration ozone water, the air diffuser (2) in the reaction cylinder A (5) is opened by opening the solenoid valve (17) provided in the flow path (7). Ozone water obtained by contacting the gas introduced further and the water sprayed from the one-liquid nozzle (4) is introduced into the storage tank B (10 ') through the flow path (7). When the water level of the ozone water in the storage tank A (10) and the storage tank B (10 ') becomes constant, a water level meter installed in the storage tank A (10)
(9) and (8) and the solenoid valve provided in the discharge path (14) according to the signals from the water level gauges (9 ') and (8') provided in the storage tank B (10 ')
Ozone water is sprayed from the discharge passage (14) through the discharge channel (14) by the pump (6 ') through the one-liquid nozzle (4) provided in the reaction tube A (5), and the ozone water comes into contact with ozone gas again. Ozone water having a high concentration can be obtained, and the ozone water in the storage tank A (10) passes through the flow path (7) via the motor-operated valve (17) and is again stored in the storage tank B (1).
0 '), and the ozone water concentration is increased by circulating it again to the reaction tube A (5). When the desired ozone water concentration is reached, pump (6) from discharge path (25) via solenoid valve (26)
Emit by. Ozone water can be intermittently obtained because the ozone water is circulated until it reaches the desired concentration. In this case, water is supplied through the water supply passage (13) -solenoid valve (15) -spray nozzle mounting pipe (3) -single-liquid nozzle (4) -reservoir A (10) -flow passage (7).
-Motorized valve (17) -Flows with the reservoir B (10 '), and when the desired amount of water is reached, the solenoid valve (15) is closed by the signal of the water level gauge (8, 9, 8', 9 ') and the pump (6 '), And circulate the stored water. At this time, the solenoid valve (15 ') is closed. On the other hand, the exhaust gas is discharged from the ozone gas passage B (12) -solenoid valve (18) -ozone killer (2
0) and the solenoid valves (18 ', 19) are closed. Furthermore,
When continuously producing ozone water so that the concentration of ozone water becomes constant in a short time, after the ozone water is discharged to the outside of the storage tank A (10) and the storage tank B (10 ') before water supply, Pump (2
2) is used to send air into the reaction tube A (5) and the reaction tube B (5 ') via the air passageway (21) and the check valve (24), and unreacted ozone gas is discharged into the exhaust ozone gas passageway (12). ) Is discharged to the ozone killer through the solenoid valve (18), and the reaction cylinder A (5) and the reaction cylinder B are discharged.
(5 ') and the amount of residual ozone gas in the storage tank A (10) and the storage tank B (10') can be maintained constant.

【0017】オゾン水製造例1反応筒A(5)及び反応筒
B(5')の寸法:内径φ70.3mm×高さ112mm貯
留槽A(10)及び貯留槽B(10')の寸法:縦100mm×
横126mm×高さ218mm前記の寸法をもつ装置を
用いて濃度60,000ppmのオゾンガスを120cc/分で
送入し、2リットル/分の水を給水したところ、6pp
m、10ppm及び15ppmの安定したオゾン水を得
た。安定したオゾン水を得るまでにかかった時間はそれ
ぞれ10分、10分及び15分であった。
Ozone Water Production Example 1 Dimensions of reaction tube A (5) and reaction tube B (5 '): inner diameter φ70.3 mm × height 112 mm Dimensions of storage tank A (10) and storage tank B (10'): Vertical 100 mm x
126 mm in width x 218 mm in height Using the device having the above dimensions, ozone gas having a concentration of 60,000 ppm was fed at 120 cc / min, and 2 liters / min of water was supplied.
m, 10 ppm and 15 ppm of stable ozone water were obtained. The time required to obtain stable ozone water was 10 minutes, 10 minutes and 15 minutes, respectively.

【0018】[0018]

【発明の効果】以上の説明から明らかなように、本発明
によれば一定濃度のオゾンガスに対し3タイプの濃度の
オゾン水を短時間に得ることができる。
As is apparent from the above description, according to the present invention, it is possible to obtain ozone water of three types of concentration for a constant concentration of ozone gas in a short time.

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

【図1】本発明のオゾン水製造システムの1実施態様を
説明する図である。
FIG. 1 is a diagram illustrating one embodiment of an ozone water production system of the present invention.

【符号の説明】[Explanation of symbols]

1、1’ 排オゾンガス通路A 2、2’ 散気具 3、3’ 噴霧ノズル取付パイプ 4、4’ 一液用ノズル 5 反応筒A 5’ 反応筒B 6、6’ ポンプ 7 流路 8、8’ 水位計 9、9’ 水位計 10 貯留槽A 10' 貯留槽B 11 オゾナイザ 12 排オゾンガス通路B 13 給水路A 13' 給水路B 14 放出路 15、15'、16 電磁弁 17 電動弁 18、19 電磁弁 20 オゾンキラー 21 空気通路 22 エアーポンプ 23、24 逆止弁 25 放出路 26 電磁弁 1, 1'Exhaust ozone gas passage A 2, 2'Diffuser 3, 3'Spray nozzle mounting pipe 4, 4'One-liquid nozzle 5 Reaction tube A 5'Reaction tube B 6, 6'Pump 7 Flow path 8, 8'Water level meter 9, 9'Water level meter 10 Storage tank A 10 'Storage tank B 11 Ozonizer 12 Exhaust ozone gas passage B 13 Water supply passage A 13' Water supply passage B 14 Discharge passage 15, 15 ', 16 Solenoid valve 17 Motorized valve 18 , 19 Solenoid valve 20 Ozone killer 21 Air passage 22 Air pump 23, 24 Check valve 25 Discharge passage 26 Solenoid valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 反応筒と、反応筒に設けられた噴霧ノズ
ルと、水を電気分解してオゾンガスを得るためのオゾナ
イザと、オゾナイザからのオゾンガスを前記反応筒内に
放出する散気具と、反応筒の下部に接続されたオゾン水
貯留槽と、得られたオゾン水を放出する液体ポンプを備
えてなる反応筒を2個以上オゾンガスと水とが向流にな
るように直列に接続し、なおかつ前記貯留槽間をオゾン
水が循環できるようにした流路を備えてなるオゾン水製
造システム。
1. A reaction tube, a spray nozzle provided in the reaction tube, an ozonizer for electrolyzing water to obtain ozone gas, and an air diffuser for discharging ozone gas from the ozonizer into the reaction tube. An ozone water storage tank connected to the lower part of the reaction tube and a reaction tube provided with a liquid pump for discharging the obtained ozone water are connected in series so that two or more ozone gas and water flow countercurrently, Furthermore, an ozone water production system comprising a flow path that allows ozone water to circulate between the storage tanks.
【請求項2】 反応筒内に空気を送り込むためのエアー
ポンプと、前記反応筒の上部に接続し、オゾンガスを分
解無害化するオゾンキラーを備えてなる請求項1記載の
オゾン水製造システム。
2. The ozone water production system according to claim 1, further comprising an air pump for feeding air into the reaction tube, and an ozone killer connected to an upper portion of the reaction tube to decompose and detoxify ozone gas.
JP3040487A 1991-02-13 1991-02-13 Ozone water production system Expired - Lifetime JPH0655311B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3040487A JPH0655311B2 (en) 1991-02-13 1991-02-13 Ozone water production system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3040487A JPH0655311B2 (en) 1991-02-13 1991-02-13 Ozone water production system

Publications (2)

Publication Number Publication Date
JPH04260496A JPH04260496A (en) 1992-09-16
JPH0655311B2 true JPH0655311B2 (en) 1994-07-27

Family

ID=12581950

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3040487A Expired - Lifetime JPH0655311B2 (en) 1991-02-13 1991-02-13 Ozone water production system

Country Status (1)

Country Link
JP (1) JPH0655311B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4469078B2 (en) * 2000-11-13 2010-05-26 コフロック株式会社 High concentration ozone water production apparatus and method for producing high concentration ozone water using this apparatus

Also Published As

Publication number Publication date
JPH04260496A (en) 1992-09-16

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