JPH0389995A - Ozone water-making apparatus - Google Patents
Ozone water-making apparatusInfo
- Publication number
- JPH0389995A JPH0389995A JP22451789A JP22451789A JPH0389995A JP H0389995 A JPH0389995 A JP H0389995A JP 22451789 A JP22451789 A JP 22451789A JP 22451789 A JP22451789 A JP 22451789A JP H0389995 A JPH0389995 A JP H0389995A
- Authority
- JP
- Japan
- Prior art keywords
- ozone
- high pressure
- pressure air
- supply part
- mixing
- 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
Links
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 70
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 claims description 15
- 239000000203 mixture Substances 0.000 abstract description 5
- 238000004090 dissolution Methods 0.000 abstract 2
- 230000000694 effects Effects 0.000 description 5
- 238000012423 maintenance Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、管中を高速で流れる水流にオゾン(O8)
を注入し混合・溶解させるためのオゾン水製造装置に関
する。[Detailed Description of the Invention] [Industrial Field of Application] This invention applies ozone (O8) to a water stream flowing at high speed in a pipe.
This invention relates to an ozone water production device for injecting, mixing and dissolving ozone water.
この種のオゾン水製造装置としては、例えば特開昭63
−200891号公報に示されるようなものがある。As this type of ozone water production device, for example, Japanese Patent Application Laid-Open No. 63
There is one as shown in Japanese Patent No.-200891.
このオゾン水製造装置は、それ以前のものが最高0.7
ppm程度の溶解度を実現できるに過ぎなかったのに比
べ、3〜5ppm(5)ン/hrの水処理量において5
g/hrのオゾン注入量)という非常に高濃度なオゾン
溶解度を達成でき、それなりに秀れたオゾン処理効果を
実現できたものである。This ozonated water production device had a maximum of 0.7
Compared to previous studies, it was only possible to achieve a solubility of about 3 ppm (ppm);
It was possible to achieve a very high concentration of ozone solubility (ozone injection amount: g/hr), and to achieve a reasonably excellent ozone treatment effect.
しかし、5ppmというオゾン溶解度は必ずしも必要十
分なものとは言えず、幾つかの研究成果によると、6p
pm以上のオゾン溶解度が得られれば、その水処理効果
は格段に向上するという知見が与えられている。However, an ozone solubility of 5 ppm is not necessarily sufficient, and according to some research results, 6 ppm
Knowledge has been given that if an ozone solubility of pm or higher is obtained, the water treatment effect will be significantly improved.
このような事情を背景に、当発明者は6ppm以上とい
う新たな溶解度の壁を破ることのできるオゾン水製造装
置について種々の改良・工夫を重ねてきたが、ここにそ
の完成をみたものである。Against this background, the present inventor has made various improvements and devises for an ozone water production device that can break the new solubility barrier of 6 ppm or more, and we have now reached the completion of these efforts. .
具体的には、この発明によるオゾン水製造装置は、源水
供給側から溶解水排出側に向けて順番にオゾン供給部、
磁気処理部及び攪拌部が設けられた処理管を備えてなる
ものである。Specifically, the ozone water production device according to the present invention includes an ozone supply section, an ozone supply section,
It is equipped with a processing tube provided with a magnetic processing section and a stirring section.
このオゾン水製造装置の特徴の一つは、磁気処環部をオ
ゾン供給部の下流に設けている点である。One of the features of this ozone water production device is that the magnetic treatment section is provided downstream of the ozone supply section.
このように磁気処理部をオゾン供給部の下流に設けるこ
とにより、その細かいメカニズムは不明なものの、オゾ
ンの混合・溶解についての磁気処理効率が向上し、より
高いオゾンの混合・溶解度を実現できたものである。By installing the magnetic processing section downstream of the ozone supply section in this way, although the detailed mechanism is unknown, the magnetic processing efficiency for mixing and dissolving ozone was improved, and higher ozone mixing and solubility was achieved. It is something.
以下、この発明の一実施例を図面に基づき説明する。 Hereinafter, one embodiment of the present invention will be described based on the drawings.
第1図に示すのは、この発明によるオゾン水製造装置l
の要部で、処理管2に、源水供給側2Sから溶解水排出
側2eに向けて、つまり上流から下流に向けて、順番に
オゾン供給部3、磁気処理部4及び攪拌部5を設けてい
る。Fig. 1 shows an ozone water production apparatus according to the present invention.
In the main part of the treatment pipe 2, an ozone supply part 3, a magnetic treatment part 4, and a stirring part 5 are provided in order from the source water supply side 2S to the dissolved water discharge side 2e, that is, from upstream to downstream. ing.
処理管2をU字状としているが、これもこの装置の特徴
の一つで、これにより装置全体の小型化が図られている
。The processing tube 2 is U-shaped, which is also one of the features of this device, and this allows the entire device to be miniaturized.
オゾン供給部3は、オゾン供給機6より供給されるオゾ
ン(オゾンガス)Oを高圧空気供給機7より供給される
高圧空気Eを利用して処理管2中の高速水流S中に注入
する部位である。The ozone supply unit 3 is a part that injects ozone (ozone gas) O supplied from the ozone supply machine 6 into the high-speed water flow S in the processing tube 2 using high pressure air E supplied from the high pressure air supply machine 7. be.
具体的には、第3図に示すように、高圧空気供給パイプ
8の先端をL字状に曲折させて噴出部8Vを形成し、こ
の噴出部8■が先端の噴出口8hを下流に向けて水流S
と平行になるように配し、さらにこの噴出部8Vに直交
するようにオゾン供給パイプ9を接続している。つまり
、オゾン供給パイプ9で供給されてくるオゾンOを、噴
出部8Vを高速で流れる高圧空気Eにより生じる負圧に
より高圧空気E中に混合させ、高圧空気オゾン混合体O
Eとし、この高圧空気オゾン混合体OEによる高圧を以
て水流S中にオゾン○を効率よく混合・溶解させるよう
にしている。Specifically, as shown in Fig. 3, the tip of the high-pressure air supply pipe 8 is bent into an L-shape to form a jetting section 8V, and this jetting section 8■ directs the jetting port 8h at the tip downstream. Water flow S
Further, an ozone supply pipe 9 is connected so as to be perpendicular to this ejection part 8V. In other words, the ozone O supplied through the ozone supply pipe 9 is mixed into the high pressure air E by the negative pressure generated by the high pressure air E flowing at high speed through the ejection part 8V, and the high pressure air ozone mixture O is mixed with the ozone O supplied through the ozone supply pipe 9.
E, and the ozone ○ is efficiently mixed and dissolved in the water stream S using the high pressure generated by this high-pressure air-ozone mixture OE.
このように、オゾンOを高圧空気オゾン混合体OEにし
て供給すると、この高圧空気オゾン混合体OEが言わば
エアーハンマー的な作用をなすので、このオゾン水製造
装置1が接続される水道管内のスライム、錆こぶ等の除
去にとって非常に有用である。In this way, when ozone O is supplied as a high-pressure air ozone mixture OE, this high-pressure air ozone mixture OE acts like an air hammer, so that the slime in the water pipe to which this ozone water production device 1 is connected is removed. , very useful for removing rust galls, etc.
第1図及び第3図中に想像線で示すのは、処理管2中を
流れる水流Sを分岐導入して分流Sdを形成するための
分岐パイプ8bである。すなわち、前述の高圧空気Eに
替えて分流Sdを高圧空気供給パイプ8に流し、この分
流Sdによる負圧によりオゾンOを高速水流S中に供給
するためのもので、この場合には前述の「エアーハンマ
ー効果」がないので、オゾンを主に殺菌用として用いる
場合に利用するものである。尚、高圧空気Eと分流Sd
の使い分けはバルブV1、V2の操作により行う。What is shown by imaginary lines in FIGS. 1 and 3 is a branch pipe 8b for branching and introducing the water flow S flowing through the processing tube 2 to form a branch flow Sd. That is, in place of the above-mentioned high-pressure air E, a divided flow Sd is flowed into the high-pressure air supply pipe 8, and ozone O is supplied into the high-speed water flow S by the negative pressure caused by this divided flow Sd. In this case, the above-mentioned " Since it does not have the "air hammer effect," ozone is mainly used for sterilization. In addition, high pressure air E and branch flow Sd
The appropriate use is made by operating valves V1 and V2.
このような混合・溶解構造によると、オゾンOを高圧で
水流S中に注入できその混合・溶解の効率を大きく高め
ることができるし、しかもオゾン供給機6において高い
圧力を発生する必要がないのでオゾン供給機6の保守・
管理が容易となるという利点が得られる。すなわち、オ
ゾン供給機6に高圧発生用として例えばポンプのような
複雑な機構を持ったものなどを設けると、オゾンの強力
な酸化力によりこれらがすぐに傷んでしまい、その保守
・管理が大変であるが、このような高圧発生用のポンプ
類を不要とすることによりオゾン供給機6の保守・管理
の容易化が達成されているものである。According to such a mixing/dissolving structure, ozone O can be injected into the water stream S at high pressure, and the mixing/dissolving efficiency can be greatly increased, and there is no need to generate high pressure in the ozone supply device 6. Maintenance of ozone supply machine 6
This has the advantage of being easier to manage. In other words, if the ozone supply device 6 is equipped with a complex mechanism such as a pump for generating high pressure, the strong oxidizing power of ozone will quickly damage these components, making maintenance and management difficult. However, by eliminating the need for such pumps for generating high pressure, maintenance and management of the ozone supply device 6 can be facilitated.
磁気処理部4をオゾン供給部3の下流に設けた点もこの
オゾン水製造装置lの特徴の一つであるが、その細かい
メカニズムは不明なものの、このように磁気処理部4を
オゾン供給部3の下流に設けることが、オゾンOの混合
・溶解についての磁気処理効率の向上、延いてはオゾン
Oの混合・溶解について大きく寄与している。One of the features of this ozonated water production apparatus l is that the magnetic processing section 4 is provided downstream of the ozone supply section 3.Although the detailed mechanism is unknown, in this way the magnetic processing section 4 is installed downstream of the ozone supply section 3. Providing it downstream of No. 3 greatly contributes to improving the magnetic processing efficiency for mixing and dissolving ozone O, and by extension, to mixing and dissolving ozone O.
この磁気処理部4は、第4図に示すように、支持リング
10の回りに複数の磁気棒11.11、を固定バンド1
2.12、−゛−゛で固定してなるもので、各磁気棒1
1.11、“−は水流Sに対し平行になるようにされて
いる。As shown in FIG.
2.12, fixed with -゛-゛, each magnetic bar 1
1.11, "- is parallel to the water flow S.
攪拌部5は、第5図に示すように、処理管2の内壁に複
数、具体的には5枚の半円状のフィン13.13、−・
・−をその取付は角度が90°ずっ順番にずれるように
して一定間隔で取り付けてなるもので、これらの半円状
のフィン13.13、により螺旋状の流路が形成され、
この螺旋状の流路を水流Sか通過することにより攪拌が
なされるようになっている。As shown in FIG. 5, the stirring section 5 includes a plurality of semicircular fins 13, 13, -
・The fins 13 and 13 are attached at regular intervals so that the angles are shifted by 90 degrees, and a spiral flow path is formed by these semicircular fins 13 and 13.
Stirring is achieved by passing the water stream S through this spiral channel.
このようなオゾン水製造装置1により達成されたオゾン
の最高溶解度は、5トン/hrの処理量において18g
/hrのオゾン注入量で、8.6ppmであった。The maximum solubility of ozone achieved by such ozone water production apparatus 1 is 18 g at a treatment rate of 5 tons/hr.
The ozone injection amount was 8.6 ppm.
この発明に係るオゾン水製造装置は、以上説明してきた
如く、源水供給側から溶解水排出側に向けて順番にオゾ
ン供給部、磁気処理部及び攪拌部が設けられた処理管を
備えてなるものであり、磁気処理部をオゾン供給部の下
流に設けることにより、従来のものに比べより高いオゾ
ンの混合・溶解度を実現できるという効果がある。As explained above, the ozone water production device according to the present invention includes a processing pipe in which an ozone supply section, a magnetic processing section, and a stirring section are provided in order from the source water supply side to the dissolved water discharge side. By providing the magnetic processing section downstream of the ozone supply section, there is an effect that higher mixing and solubility of ozone can be achieved than in conventional systems.
第1図は、オゾン水製造装置の要部である処理管の簡略
図、
第2図は、処理管の概略側面図、
第3図は、第2図中の矢示■方向からみた処理管の一部
断面を含む概略側面図、
第4図は、第3図中の矢示■
半断面図、そして
第5図は、攪拌部の概略断面図である。
1−−−−−−−オゾン水製造装置
2−・・・−処理管
2 s −−−−−一一一源水供給側
2 e −一溶解水排出側
3−−−・・オゾン供給部
4−一一一一一一磁気処理部
5−−−−−−−一攪拌部
■線に沿う概略
特開平
3
89995 (4)Figure 1 is a simplified diagram of the processing tube, which is the main part of the ozone water production equipment. Figure 2 is a schematic side view of the treatment tube. Figure 3 is the treatment tube seen from the direction of the arrow ■ in Figure 2. 4 is a schematic side view including a partial cross section, FIG. 4 is a half sectional view taken along the arrow (1) in FIG. 3, and FIG. 5 is a schematic sectional view of the stirring section. 1 ------- Ozonated water production device 2 - Processing pipe 2 s ----1 Source water supply side 2 e -1 Dissolved water discharge side 3 ---- Ozone supply Part 4-11111 Magnetic processing part 5-----1 Stirring part ■ Schematic along the line JP-A-3-89995 (4)
Claims (1)
部、磁気処理部及び攪拌部が設けられた処理管を備えて
なるオゾン水製造装置。An ozonated water production device comprising a processing pipe in which an ozone supply section, a magnetic processing section, and a stirring section are provided in order from the source water supply side to the dissolved water discharge side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22451789A JPH0389995A (en) | 1989-09-01 | 1989-09-01 | Ozone water-making apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22451789A JPH0389995A (en) | 1989-09-01 | 1989-09-01 | Ozone water-making apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0389995A true JPH0389995A (en) | 1991-04-15 |
Family
ID=16815036
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22451789A Pending JPH0389995A (en) | 1989-09-01 | 1989-09-01 | Ozone water-making apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0389995A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0639196U (en) * | 1992-11-02 | 1994-05-24 | トヨシマ電機株式会社 | Water purification equipment |
US5971368A (en) * | 1997-10-29 | 1999-10-26 | Fsi International, Inc. | System to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized |
US6235641B1 (en) | 1998-10-30 | 2001-05-22 | Fsi International Inc. | Method and system to control the concentration of dissolved gas in a liquid |
US6274506B1 (en) | 1999-05-14 | 2001-08-14 | Fsi International, Inc. | Apparatus and method for dispensing processing fluid toward a substrate surface |
US6406551B1 (en) | 1999-05-14 | 2002-06-18 | Fsi International, Inc. | Method for treating a substrate with heat sensitive agents |
-
1989
- 1989-09-01 JP JP22451789A patent/JPH0389995A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0639196U (en) * | 1992-11-02 | 1994-05-24 | トヨシマ電機株式会社 | Water purification equipment |
US5971368A (en) * | 1997-10-29 | 1999-10-26 | Fsi International, Inc. | System to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized |
US6488271B1 (en) * | 1997-10-29 | 2002-12-03 | Fsi International, Inc. | Method to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized |
US6648307B2 (en) | 1997-10-29 | 2003-11-18 | Fsi International, Inc. | Method to increase the quantity of dissolved gas in a liquid and to maintain the increased quantity of dissolved gas in the liquid until utilized |
US6235641B1 (en) | 1998-10-30 | 2001-05-22 | Fsi International Inc. | Method and system to control the concentration of dissolved gas in a liquid |
US6274506B1 (en) | 1999-05-14 | 2001-08-14 | Fsi International, Inc. | Apparatus and method for dispensing processing fluid toward a substrate surface |
US6406551B1 (en) | 1999-05-14 | 2002-06-18 | Fsi International, Inc. | Method for treating a substrate with heat sensitive agents |
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