JPS63166493A - Apparatus for making ozone dissolved water - Google Patents

Apparatus for making ozone dissolved water

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Publication number
JPS63166493A
JPS63166493A JP31250886A JP31250886A JPS63166493A JP S63166493 A JPS63166493 A JP S63166493A JP 31250886 A JP31250886 A JP 31250886A JP 31250886 A JP31250886 A JP 31250886A JP S63166493 A JPS63166493 A JP S63166493A
Authority
JP
Japan
Prior art keywords
water
ozone
mixing chamber
dissolved
dissolved water
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
JP31250886A
Other languages
Japanese (ja)
Other versions
JPH0239955B2 (en
Inventor
Katsumi Takao
高尾 克己
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP31250886A priority Critical patent/JPH0239955B2/en
Publication of JPS63166493A publication Critical patent/JPS63166493A/en
Publication of JPH0239955B2 publication Critical patent/JPH0239955B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To freely enhance an ozone dissolving ratio, by mounting a mixing chamber for contacting and mixing water with ozone and by providing a grinding means for finely pulverizing water in the mixing chamber. CONSTITUTION:The water sent into a mixing chamber 7 under pressure by a pressure feed means 4 is injected from a large number of the nozzles arranged to the entire inner wall surface of the mixing chamber 7 and finely pulverized to be formed into mist to fill the mixing chamber 7. Ozone is present in the mixing chamber 7 and violently collides with fine water particles fed in the mixing chamber 7 under pressure to be brought into contact with a mist of water many-sidedly at extremely high density. As a result, the fine water particles grow to water droplets having a large amount of ozone dissolved therein to be accumulated on the bottom part of the mixing chamber 7 and supplied as high concn. ozone dissolved water from an outlet 9. By this method, an ozone dissolving ratio can be freely adjusted.

Description

【発明の詳細な説明】 し産業上の利用分野] この発明は食品加工・解凍処理等に用いられる無菌水の
供給、あるいは飲料水の脱臭・滅菌、冷却水の浄化等に
おいて利用される、水にオゾンを溶解させる装置に関す
る。より具体的には、水を強制的にオゾンに接触させて
オゾン溶解水を製造する装置に関する。
[Detailed Description of the Invention] Industrial Application Field] The present invention is directed to the supply of sterile water used in food processing, thawing, etc., the deodorization and sterilization of drinking water, the purification of cooling water, etc. This invention relates to a device for dissolving ozone. More specifically, the present invention relates to an apparatus for producing ozone-dissolved water by forcibly bringing water into contact with ozone.

[従来技術] 従来のオゾン溶解水の製造装置としては、貯溜した水の
水底付近からオゾンを供給して、水中を上昇するオゾン
の気゛泡で水に接触させ、これによってオゾンを水に溶
解させることが知られている。
[Prior art] Conventional ozone-dissolved water production equipment supplies ozone from near the bottom of stored water, contacts the water with ozone bubbles rising in the water, and thereby dissolves ozone in the water. It is known to cause

[発明が解決しようとする問題点] しかるに従来の方法によるときは、水とオゾンとの接触
が強制的・積極的でなく、また、水とオゾンとの接触面
積は極めて限られていたため、オゾンは十分に水中に溶
解することができず、オゾン溶解率を高めることが困難
であった。
[Problems to be solved by the invention] However, when using the conventional method, the contact between water and ozone was not forced or positive, and the contact area between water and ozone was extremely limited. could not be sufficiently dissolved in water, making it difficult to increase the ozone dissolution rate.

また、従来方法によるオゾン溶解水製造装置にあっては
オゾン溶解率を自在に調整することも困難であった。し
たがって用途に応じたオゾン溶解水を得ることが難しか
った。
Furthermore, in the conventional method for producing ozone-dissolved water, it is difficult to freely adjust the ozone dissolution rate. Therefore, it has been difficult to obtain ozone-dissolved water suitable for various uses.

[発明の目的コ この発明は上記問題点を解決し、オゾン溶解率を自在に
高め、かつ、オゾン溶解率を容易に高低調節することが
できるオゾン溶解水製造装置を提供することを目的とす
る。
[Purpose of the Invention] An object of the present invention is to solve the above-mentioned problems, and to provide an ozone-dissolved water production device that can freely increase the ozone dissolution rate and easily adjust the ozone dissolution rate. .

[問題点を解決するための手段] 上記目的を達成するため、本発明に係るオゾン溶解水製
造装置は、水とオゾンとを接触混合する混合室と、同混
合室内に設けられた水を微粒子化する粉砕手段と、同粉
砕手段に接続された水の圧送手段と、混合室に接続され
たオゾンの圧送手段とからなる構成としている。
[Means for Solving the Problems] In order to achieve the above object, the ozone-dissolved water production device according to the present invention includes a mixing chamber for contact-mixing water and ozone, and a mixing chamber for mixing water with fine particles. The apparatus is constructed of a crushing means for pulverizing, a means for pumping water connected to the crushing means, and a means for pumping ozone connected to a mixing chamber.

[実施例] 以下、本発明の実施例につき、図面を参照して詳細に説
明する。
[Example] Hereinafter, examples of the present invention will be described in detail with reference to the drawings.

第1図は本発明に係るオゾン溶解水製造装置による水お
よびオゾンの流れを示す概念図である。1は水源であっ
て、バルブ2、フィルタ3を介して圧送手段4と結ばれ
、さらに、水量調整弁5、Affi計6を介して混合室
7と結ばれている。上記圧送手段4は水源1から水を吸
引して混合室7内に水を送り込むもので、具体的には、
例えばポンプである。
FIG. 1 is a conceptual diagram showing the flow of water and ozone by the ozone-dissolved water production apparatus according to the present invention. Reference numeral 1 denotes a water source, which is connected to a pressure feeding means 4 via a valve 2 and a filter 3, and further connected to a mixing chamber 7 via a water volume adjustment valve 5 and an Affi meter 6. The pressure feeding means 4 sucks water from the water source 1 and sends the water into the mixing chamber 7. Specifically,
For example, a pump.

一方、10はオゾン源であって、具体的には酸素もしく
は空気である。このオゾン源10は圧送手段11.バル
ブ12、フィルタ13を介してオゾナイザ14と結ばれ
、さらに、オゾン1m8整弁15を介して上記混合室7
と結ばれている。ここで上記オゾン源10として圧縮酸
素を使用すれば次のような効果がある。すなわちボンベ
中に詰め込まれた純度の高い酸素を利用でき、空気から
オゾンを製造する手間やコストを省はオゾンが容易に人
手できる。圧送手段11を特別に設ける手間やコストも
省ける。さらにまた、空気からオゾンを製造する場合の
酸化窒素物の発生を防止でき、毒性を排除できる、とい
う種々の利点がある。上記オゾナイザ14は一般の無声
放電によるオゾン製造装置であるが、ここでは高純度ア
ルミナセラミック層にプリントした電極による沿面放電
式のものを採用くし している。オゾン源lOはフィルターを介して塵芥を除
去された後、オゾナイザ14によって1部オゾンにされ
、オゾン化されていない残部の酸素と共に混合室7内に
送り込まれる。この送り込みの圧送手段11はオゾン源
IOに付属の圧縮力である。
On the other hand, 10 is an ozone source, specifically oxygen or air. This ozone source 10 is connected to a pressure feeding means 11. It is connected to an ozonizer 14 via a valve 12 and a filter 13, and is further connected to the mixing chamber 7 via an ozone 1m8 regulating valve 15.
It is tied to Here, if compressed oxygen is used as the ozone source 10, the following effects can be obtained. In other words, highly pure oxygen packed in a cylinder can be used, and the labor and cost of producing ozone from air can be saved, and ozone can be easily produced manually. The effort and cost of specially providing the pressure feeding means 11 can also be saved. Furthermore, there are various advantages such as being able to prevent the generation of nitrogen oxides and eliminating toxicity when producing ozone from air. The ozonizer 14 is a general ozone production device using silent discharge, but here a creeping discharge type using electrodes printed on a high-purity alumina ceramic layer is employed. After dust is removed from the ozone source 10 through a filter, a portion of the ozone source 1O is converted into ozone by an ozonizer 14 and sent into the mixing chamber 7 together with the remaining non-ozonized oxygen. The pumping means 11 for this feeding is a compressive force attached to the ozone source IO.

次に第2図は、水を微粒子化する粉砕手段の1実施例を
示す。粉砕手段8は多数のノズルを混合室7内の全壁面
に配設させて成るもので、第2図および第1図において
、水は圧送手段4によって流量計6を経て混合室7内に
圧送されてくると混合室7内の全壁面に配設された多数
のノズルから噴出して微粒子化され霧状になって混合室
7内に充満する。一方オシンは、混合室7内にあって、
同室7内に圧送され来り飛散し衝突し合う水の微粒子に
激しく衝突して、極めて高密度、多面的に霧状の水と接
触し合う。
Next, FIG. 2 shows an embodiment of a crushing means for turning water into fine particles. The crushing means 8 is composed of a large number of nozzles arranged on the entire wall surface of the mixing chamber 7, and in FIGS. When the mixture is mixed, it is ejected from a large number of nozzles arranged on the entire wall surface of the mixing chamber 7, and the mixing chamber 7 is filled with the atomized atomized particles. On the other hand, the oil is in the mixing chamber 7,
The particles violently collide with the water particles that are pumped into the same chamber 7, scatter, and collide with each other, and come into contact with extremely high-density, multifaceted mist water.

その結果微粒子状の水はオゾンを多量に溶解した水滴と
なって混合室7の底部に溜まり、アウトレット9から高
濃度のオゾン溶解水として供給される。この場合、水の
圧送手段4、オゾンの圧送手段11.オゾイナイザ14
、あるいは粉砕手段8の力率またはオゾン量調整弁15
、水ffl調整弁5を調節することにより、水中のオゾ
ン溶解率を調整することかり能である。。
As a result, the particulate water becomes water droplets containing a large amount of ozone dissolved therein and accumulates at the bottom of the mixing chamber 7, and is supplied from the outlet 9 as highly concentrated ozone-dissolved water. In this case, the water pumping means 4, the ozone pumping means 11. Ozoinizer 14
, or the power factor of the crushing means 8 or the ozone amount adjusting valve 15
By adjusting the water ffl adjustment valve 5, it is possible to adjust the ozone dissolution rate in water. .

次に第3図は別の実施例を示す概念図であるが、この第
2実施例では水源1を上記第1実施例で製造したオゾン
溶解水としており、既にオゾンを溶解した水を再びオゾ
ンと混合させることにより、オゾン濃度を高める構成に
している。
Next, FIG. 3 is a conceptual diagram showing another embodiment. In this second embodiment, the water source 1 is the ozone-dissolved water produced in the first embodiment, and the water in which ozone has already been dissolved is re-ozone-dissolved. By mixing with ozone, the ozone concentration is increased.

この場合、単に上記第1実輿例で製造したオゾン溶解水
を再度、同一製造装置内に循環させる構成も可能である
が、ここに記載の第2実施例では、第3図に見られるよ
うa÷、水源lは、バルブ2、フィルタ3を経由して貯
水槽20内に一旦貯蔵させる構成としている。貯水槽2
0内には前記の混合室7が粉砕手段8と共に設置されて
おり、この混合室7のアウトレット9には水中管21が
接続され、水中管21は貯水槽20の底部箇所にまで伸
びて、同所において解放されている。すなわちアウトレ
ット9から出るオゾン溶解水は水中管2Iによって貯水
槽20の底部にまで導かれている。貯水槽20は、近隣
に設置された水位調整[22とそれら水槽の側壁上下に
複数設けられた連通管23によって互いに連通されてい
る。水位調整槽22にはレベルスイッチ24が取り付け
られ、同レベルスイッチ24からは上記連通管23の数
に等しい本数のレベルセンサ25が各連通管23の最下
端より僅かに下方に来る水面を感知できるように各々伸
びている。そしてレベルセンサ25に感知された水位は
、レベルスイッチ24を介して接続されたバルブ2に信
号を送って水位の各段階ごとにバルブ2を開閉するよう
にされている。なお、ここにバルブ2は電磁弁である。
In this case, it is also possible to simply circulate the ozone-dissolved water produced in the above-mentioned first example within the same production equipment, but in the second embodiment described here, as shown in FIG. The water source l is temporarily stored in a water tank 20 via a valve 2 and a filter 3. Water tank 2
The mixing chamber 7 is installed together with the crushing means 8 in the mixing chamber 7, and an underwater pipe 21 is connected to the outlet 9 of the mixing chamber 7, and the underwater pipe 21 extends to the bottom of the water tank 20. He was released at the same location. That is, the ozone-dissolved water coming out of the outlet 9 is led to the bottom of the water storage tank 20 by the underwater pipe 2I. The water tanks 20 are communicated with each other by a water level adjuster 22 installed nearby and a plurality of communication pipes 23 provided above and below the side walls of the water tanks. A level switch 24 is attached to the water level adjustment tank 22, and from the same level switch 24, a number of level sensors 25 equal to the number of communicating pipes 23 can detect the water surface slightly below the lowest end of each communicating pipe 23. Each of them is growing like this. The water level sensed by the level sensor 25 sends a signal to the valve 2 connected via the level switch 24 to open and close the valve 2 at each stage of the water level. Note that the valve 2 here is a solenoid valve.

また、水位調整槽22の上縁近傍からはオーバーフロー
管29が引き出されて、余分な水を排出できるようにさ
れている。
Further, an overflow pipe 29 is drawn out from near the upper edge of the water level adjustment tank 22 so that excess water can be discharged.

水はこの水位調整槽22の最下水位置に開口された排水
口26から出ると、丁字配管の先に設置されたコック2
7もしくは給水栓28が閉じられていれば、圧送手段4
に吸引されるようにされている。圧送手段4は吸引した
水を再び混合室7内に送り込み粉砕手段8を介して微粒
子化し再度混合室7内のオゾンと強制接触させる。この
ようにしてオゾンは、繰り返し溶解濃度を高められる。
When the water comes out from the drain port 26 opened at the lowest water position of the water level adjustment tank 22, a cock 2 installed at the end of the T-shaped pipe
7 or if the water tap 28 is closed, the pressure feeding means 4
It is designed to be attracted to. The pressure feeding means 4 feeds the sucked water into the mixing chamber 7 again, and the water is pulverized into fine particles through the crushing means 8 and brought into forced contact with the ozone in the mixing chamber 7 again. In this way, ozone can be repeatedly increased in dissolved concentration.

オゾン溶解水の使用に当たっては、コック27を開けて
おいて給水栓28を操作する。
When using ozone-dissolved water, the cock 27 is opened and the water tap 28 is operated.

なお、給水栓28と水源lのバルブ2の両方を閉じてお
けばオゾン溶解水の循環を無限Iこ繰り返ずことができ
るから、オゾン溶解率を高めることが可能である。
Note that if both the water tap 28 and the valve 2 of the water source 1 are closed, the circulation of the ozone-dissolved water can be repeated an infinite number of times, so it is possible to increase the ozone dissolution rate.

次に第4図は、第3実施例を示す概念図であるが、この
第3実施例は、上記第1または第2実施例で製造したオ
ゾン溶解水を自動的・継続的に氷結させる製氷装置に関
する。すなわち第4図において、製造されたオゾン溶解
水は、電磁弁30を介して接続された密閉タンク31内
に一旦貯溜される。この密閉タンク31は、その底部に
開口された給水口32を経て製氷機33に接続され、オ
ゾン溶解水が常に製氷機33へと一定量給水され続けら
れるようにされている。密閉タンク31にはレベルスイ
ッチ34が設置されており、タンク内の水量が残り少な
くなるとスイッチオンして前記電磁弁30を開きオゾン
溶解水を密閉タンク31内へと送り込む。
Next, FIG. 4 is a conceptual diagram showing the third embodiment. This third embodiment is an ice making system that automatically and continuously freezes the ozone-dissolved water produced in the first or second embodiment. Regarding equipment. That is, in FIG. 4, the produced ozone-dissolved water is temporarily stored in a closed tank 31 connected via a solenoid valve 30. This sealed tank 31 is connected to the ice maker 33 through a water supply port 32 opened at the bottom thereof, so that a fixed amount of ozone-dissolved water is constantly supplied to the ice maker 33. A level switch 34 is installed in the closed tank 31, and when the amount of water in the tank becomes low, the switch is turned on to open the electromagnetic valve 30 and send ozone-dissolved water into the closed tank 31.

そして水量が適量になるとスイッチオフして電磁弁30
を閉じる。さらに水量が溢れそうにまで送り込まれてき
た場合には、密閉タンク31内の最上部近傍に開口部を
有するオーバーフロー管35に余分な水が入り後述の排
水管38と合流して排出される。製氷機33はストッカ
36と接続されオゾン溶解水による水が貯蔵される。こ
のストッカ36にもレベルスイッチ37が設置されてい
て、氷が一定量を越えるとスイッチオンして接続の電磁
弁30を閉じ、また、一定量以下になるとスイッチオフ
して電磁弁3Gを開くようにされている。38は排水管
であって、ストッカ36内の氷解水を排出する管である
Then, when the water level reaches the appropriate level, the switch is turned off and the solenoid valve 30
Close. Furthermore, when the amount of water is fed to the point where it is about to overflow, the excess water enters an overflow pipe 35 having an opening near the top of the closed tank 31, joins with a drain pipe 38 to be described later, and is discharged. The ice maker 33 is connected to a stocker 36 to store water made from ozone-dissolved water. A level switch 37 is also installed in this stocker 36, and when the ice exceeds a certain amount, it turns on and closes the connected solenoid valve 30, and when the ice falls below a certain amount, it turns off and opens the solenoid valve 3G. is being used. 38 is a drain pipe, which is a pipe for discharging the ice-melting water in the stocker 36.

[発明の効果コ 既に以上の説明から明らかな通り、本発明のオゾン溶解
水製造装置によれば、水中へのオゾン溶解濃度を著しく
高めることができ、かつ、水の圧送手段とか、粉砕手段
、オゾナイザ等の各構成要素の力率を自在に調整できる
から、オゾン溶解率を自在に調整゛できるという効果が
ある。更に、本発明のオゾン溶解水製造装置は構造が簡
素であるから、製造コスト、メンテナンスコストが少な
くて済み、経済的であるという効果もある。
[Effects of the Invention] As is clear from the above description, the ozone-dissolved water production apparatus of the present invention can significantly increase the concentration of ozone dissolved in water, and the water pumping means, crushing means, Since the power factor of each component such as the ozonizer can be adjusted freely, there is an effect that the ozone dissolution rate can be adjusted freely. Furthermore, since the ozone-dissolved water production apparatus of the present invention has a simple structure, manufacturing costs and maintenance costs are low, and it has the effect of being economical.

また、上記第3実施例のオゾン溶解水製造装置によれば
、オゾン溶解水から自動的・継続的に製氷することがで
きるから、所望濃度のオゾン溶解水から製造された氷を
手間なく、便利、かつ、経済的に得ることができる。そ
してこの装置で製造された濃度の高いオゾン溶解水は、
これを生鮮食品や冷凍食品の輸送等につき使用して、食
品鮮度を長く維持させるという効果もある。すなわちオ
ゾン溶解水による水が氷解するにつれ小出しに発生する
オゾンにより、食品の殺菌を長時間持続することができ
るからである。
Furthermore, according to the ozone-dissolved water production apparatus of the third embodiment, ice can be made automatically and continuously from ozone-dissolved water, so ice produced from ozone-dissolved water of a desired concentration can be produced easily and conveniently. , and can be obtained economically. The highly concentrated ozone dissolved water produced with this equipment is
It can also be used to transport fresh and frozen foods, and has the effect of maintaining food freshness for a long time. In other words, the ozone generated in small amounts as the ozone-dissolved water melts the ice can sustain food sterilization for a long time.

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

第1図は本発明の第1実施例を示し、オゾン溶解水製造
装置による水およびオゾンの流れを示す概念図である。 第2図は第1実施例中の混合室および粉砕手段を示す断
面図である。第3図は同第2実施例を示し、水およびオ
ゾンの流れの概念図である。第4図は同第3実施例を示
し、オゾン溶解水を用いて自動的・継続的に製氷する装
置の概念図である。 l・・・水源 7・・・混合室 8・・・粉砕手段 10・・オゾン源 1里・・圧送手段 ・ 14・・オゾナイザ 20・・貯水槽 22・・水位調整槽 31・・密閉タンク 33・・製氷機 特許出願人   高 尾 克 己 鈴木秀太部 代理人弁理士  小 林 孝 次 第1図
FIG. 1 shows a first embodiment of the present invention, and is a conceptual diagram showing the flow of water and ozone by an ozone-dissolved water production apparatus. FIG. 2 is a sectional view showing the mixing chamber and crushing means in the first embodiment. FIG. 3 shows the second embodiment and is a conceptual diagram of the flow of water and ozone. FIG. 4 shows the third embodiment, and is a conceptual diagram of an apparatus for automatically and continuously making ice using ozone-dissolved water. l...Water source 7...Mixing chamber 8...Crushing means 10...Ozone source 1ri...Forcing means 14...Ozonizer 20...Water tank 22...Water level adjustment tank 31...Hermetically sealed tank 33 ...Ice maker patent applicant: Katsutoshi Takao; Patent attorney representing Shuta Suzuki: Takashi Kobayashi (Figure 1)

Claims (2)

【特許請求の範囲】[Claims] (1)水とオゾンとを接触混合する混合室と、同混合室
内に設けられた水を微粒子化する粉砕手段と、同粉砕手
段に接続された水の圧送手段と、混合室に接続されたオ
ゾンの圧送手段とからなるオゾン溶解水製造装置。
(1) A mixing chamber for contact-mixing water and ozone, a pulverizing means for atomizing water provided in the mixing chamber, a means for pumping water connected to the pulverizing means, and a means connected to the mixing chamber. An ozone-dissolved water production device consisting of an ozone pumping means.
(2)原水がオゾン溶解水である特許請求の範囲第1項
に記載のオゾン溶解水製造装置。
(2) The ozone-dissolved water production apparatus according to claim 1, wherein the raw water is ozone-dissolved water.
JP31250886A 1986-12-29 1986-12-29 OZONYOKAISUISEIZOSOCHI Expired - Lifetime JPH0239955B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31250886A JPH0239955B2 (en) 1986-12-29 1986-12-29 OZONYOKAISUISEIZOSOCHI

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31250886A JPH0239955B2 (en) 1986-12-29 1986-12-29 OZONYOKAISUISEIZOSOCHI

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP20557291A Division JPH05196330A (en) 1991-07-22 1991-07-22 Apparatus for making ice containing dissolved ozone

Publications (2)

Publication Number Publication Date
JPS63166493A true JPS63166493A (en) 1988-07-09
JPH0239955B2 JPH0239955B2 (en) 1990-09-07

Family

ID=18030062

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31250886A Expired - Lifetime JPH0239955B2 (en) 1986-12-29 1986-12-29 OZONYOKAISUISEIZOSOCHI

Country Status (1)

Country Link
JP (1) JPH0239955B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02198693A (en) * 1989-01-27 1990-08-07 Apanasu:Kk Ozone water cleaner
JPH03135498A (en) * 1989-10-19 1991-06-10 Japan Steel Works Ltd:The Ozone reactor
JPH03154691A (en) * 1989-11-10 1991-07-02 Permelec Electrode Ltd Method and apparatus for making high concentration ozone water
JPH04265197A (en) * 1991-02-21 1992-09-21 Japan Steel Works Ltd:The Production of aqueous ozone and equipment therefor
JP2004337846A (en) * 2003-04-14 2004-12-02 Tatsuo Okazaki Aerated water preparation method and apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02198693A (en) * 1989-01-27 1990-08-07 Apanasu:Kk Ozone water cleaner
JPH03135498A (en) * 1989-10-19 1991-06-10 Japan Steel Works Ltd:The Ozone reactor
JPH03154691A (en) * 1989-11-10 1991-07-02 Permelec Electrode Ltd Method and apparatus for making high concentration ozone water
JPH04265197A (en) * 1991-02-21 1992-09-21 Japan Steel Works Ltd:The Production of aqueous ozone and equipment therefor
JP2004337846A (en) * 2003-04-14 2004-12-02 Tatsuo Okazaki Aerated water preparation method and apparatus

Also Published As

Publication number Publication date
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