JPH0239955B2 - OZONYOKAISUISEIZOSOCHI - Google Patents

OZONYOKAISUISEIZOSOCHI

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Publication number
JPH0239955B2
JPH0239955B2 JP31250886A JP31250886A JPH0239955B2 JP H0239955 B2 JPH0239955 B2 JP H0239955B2 JP 31250886 A JP31250886 A JP 31250886A JP 31250886 A JP31250886 A JP 31250886A JP H0239955 B2 JPH0239955 B2 JP H0239955B2
Authority
JP
Japan
Prior art keywords
water
ozone
dissolved
mixing chamber
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.)
Expired - Lifetime
Application number
JP31250886A
Other languages
Japanese (ja)
Other versions
JPS63166493A (en
Inventor
Katsumi Takao
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
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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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Description

【発明の詳細な説明】 [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
つ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つた。また、従
来方法によるオゾン溶解水製造装置にあつてはオ
ゾン溶解率を自在に調整することも困難であつ
た。したがつて用途に応じたオゾン溶解水を得る
ことが難しかつた。
[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. Furthermore, in the conventional method for producing ozone-dissolved water, it has been 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] 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
調整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。
[Object of the invention] The object of the present invention is to solve the above-mentioned problems and 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は水源であつて、バルブ2、フイルタ3を介し
て圧送手段4と結ばれ、さらに、水量調整弁5、
流量計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 includes a water flow regulating valve 5,
It is connected to a mixing chamber 7 via a flow meter 6. The pressure feeding means 4 sucks water from the water source 1 and sends the water into the mixing chamber 7, and is specifically, for example, a pump.

一方、10はオゾン源であつて、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、フイルタ13を介してオ
ゾナイザ14と結ばれ、さらに、オゾン量調整弁
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けオゾンが容易
に入手できる。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
ミツク層にプリントした電極による沿面放電式の
ものを採用している。オゾン源10はフイルタ1
3を介して塵芥を除去された後、オゾナイザ14
によつて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10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 an ozonizer 14 via a pressure feeding means 11, a valve 12, and a filter 13, and is further connected to the mixing chamber 7 via an ozone amount adjustment valve 15. 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, the effort and cost of producing ozone from air can be saved, and ozone can be easily obtained. The effort and cost of specially providing the pressure feeding means 11 can also be saved. Furthermore, it is possible to prevent the generation of nitrogen oxides when producing ozone from air.
It has various advantages such as eliminating toxicity. 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 adopted. Ozone source 10 is filter 1
After the dust is removed through the ozonizer 14
A portion of the ozone is converted into ozone by the process, and the ozone is sent into the mixing chamber 7 together with the remaining oxygen that has not been ozonated.
The pumping means 11 for this feeding is a compressive force attached to the ozone source 10.

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によつて
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つて混合室7内に
充満する。一方オゾンは、混合室7内にあつて、
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。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つて混合室7の
底部に溜まり、アウトレツト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1
4、あるいは粉砕手段8の力率またはオゾン量調
整弁15、水量調整弁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が可能であ
る。
Next, Figure 2 shows one of the crushing means for turning water into fine particles.
An example is shown. The crushing means 8 is composed of a large number of nozzles arranged on the entire wall surface of the mixing chamber 7. In FIGS. When the mixture is fed under pressure, it is ejected from a large number of nozzles arranged on the entire wall surface of the mixing chamber 7, and is atomized into a mist, which fills the mixing chamber 7. On the other hand, ozone 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. 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, the ozonizer 1
4, or by adjusting the power factor of the crushing means 8, the ozone amount adjustment valve 15, and the water amount adjustment valve 5,
It is possible to adjust the rate of ozone dissolution 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、概にオゾン
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。この場
合、単に上記第1実施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
に見られるように、水源1は、バルブ2、フイル
タ3を経由して貯水槽20内に一旦貯蔵有させる
構成としている。貯水槽20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のアウトレツト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
ウトレツト9から出るオゾン溶解水は水中管21
によつて貯水槽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槽22
とそれら水槽の側壁上下に複数設けられた連通管
23によつて互いに連通されている。水位調整槽
22にはレベルスイツチ24が取り付けられ、同
レベルスイツチ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、レベルスイツチ24を介して
接続されたバルブ2に信号を送つて水位の各段階
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。また、水位
調整槽22の上縁近傍からはオーバーフロー管2
9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。
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 generally the ozone-dissolved water is reused again. By mixing it with ozone, the ozone concentration is increased. In this case, it is also possible to simply circulate the ozone-dissolved water produced in the first embodiment in the same production equipment, but in the second embodiment described here, as shown in FIG. The water source 1 is temporarily stored in a water tank 20 via a valve 2 and a filter 3. In the water storage tank 20, the mixing chamber 7 is installed together with the crushing means 8, and the outlet 9 of the mixing chamber 7 is connected to a submersible pipe 21, which extends to the bottom of the water tank 20. He was released at the same location. In other words, the ozone-dissolved water coming out of the outlet 9 is sent to the underwater pipe 21.
It is guided to the bottom of the water tank 20 by.
The water tank 20 is a water level adjustment tank 22 installed nearby.
and are connected to each other by a plurality of communication pipes 23 provided above and below the side walls of the water tank. 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, so that the valve 2 is opened or closed at each stage of the water level. Note that the valve 2 here is a solenoid valve. In addition, an overflow pipe 2 is connected from near the upper edge of the water level adjustment tank 22.
9 is pulled out to allow excess water to drain.

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、T字配管の先に設置
されたコツク27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。
オゾン溶解水の使用に当たつては、コツク27を
開けておいて給水栓28を操作する。
When the water exits from the drain port 26 opened at the lowermost position of the water level adjustment tank 22, it is sucked into the pressure feeding means 4 if the water tap 27 or water tap 28 installed at the end of the T-shaped pipe is closed. It is designed to be 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.
When using ozone-dissolved water, the pot 27 is opened and the water tap 28 is operated.

なお、給水栓28と水源1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に繰り返
すことができるから、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 infinitely, so that the ozone dissolution rate can be increased.

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
はレベルスイツチ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ツチオンして前
記電磁弁30を開きオゾン溶解水を密閉タンク3
1内へと送り込む。そして水量が適量になるとス
イツチオフして電磁弁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
ツカ36と接続されオゾン溶解水による氷が貯蔵
される。このストツカ36にもレベルスイツチ3
7が設置されていて、氷が一定量を越えるとスイ
ツ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ツチオフして電磁弁30を
開くようにされている。38は排水管であつて、
ストツカ36内の氷解力を排出する管である。
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 sealed tank 31, and when the amount of water in the tank becomes low, the switch is turned on to open the solenoid valve 30 and transfer the ozone-dissolved water to the sealed tank 3.
Send it inside 1. When the amount of water reaches an appropriate level, the switch is turned off and the solenoid valve 30 is closed. 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 ice made from ozone-dissolved water. This stocker 36 also has a level switch 3.
7 is installed, and when the amount of ice exceeds a certain amount, the switch is turned on to close the connected solenoid valve 30, and when the amount of ice is below a certain amount, the switch is turned off and the solenoid valve 30 is opened. 38 is a drain pipe,
This is a pipe that discharges the ice-melting power inside the stocker 36.

[発明の効果] 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 already clear from the above description, according to the ozone-dissolved water production apparatus of the present invention, the concentration of ozone dissolved in water can be significantly increased, and 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氷装置
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
ゾン溶解水による氷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 ice-making 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 easily and conveniently made. , and can be obtained economically. The highly concentrated ozone-dissolved water produced by this device can also be used to transport fresh and frozen foods, thereby maintaining the freshness of the foods for a long time. In other words, the ozone generated in small amounts as the ice melts due to the ozone-dissolved water allows food to be sterilized for a long time.

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

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。 1……水源、4……圧送手段、6……流量計、
7……混合室、8……粉砕手段、10……オゾン
源、11……圧送手段、14……オゾナイザ、2
0……貯水槽、22……水位調整槽、31……密
閉タンク、33……製氷機。
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. 1... Water source, 4... Pressure feeding means, 6... Flow meter,
7...Mixing chamber, 8...Crushing means, 10...Ozone source, 11...Forcing means, 14...Ozonizer, 2
0...Water tank, 22...Water level adjustment tank, 31...Airtight tank, 33...Ice maker.

Claims (1)

【特許請求の範囲】 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。 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。
[Claims] 1. A mixing chamber for contact-mixing water and ozone, a pulverizing means provided in the mixing chamber for pulverizing water, a means for pumping water connected to the pulverizing means, and a mixing chamber. An ozone-dissolved water production device consisting of an ozone pumping means connected to a 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 JPS63166493A (en) 1988-07-09
JPH0239955B2 true JPH0239955B2 (en) 1990-09-07

Family

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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)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH064158B2 (en) * 1989-01-27 1994-01-19 株式会社アパナス Ozone water purifier
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
JPS63166493A (en) 1988-07-09

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