JPH0323358Y2 - - Google Patents
Info
- Publication number
- JPH0323358Y2 JPH0323358Y2 JP15780588U JP15780588U JPH0323358Y2 JP H0323358 Y2 JPH0323358 Y2 JP H0323358Y2 JP 15780588 U JP15780588 U JP 15780588U JP 15780588 U JP15780588 U JP 15780588U JP H0323358 Y2 JPH0323358 Y2 JP H0323358Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- pool
- tank
- circuit
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 32
- 238000000746 purification Methods 0.000 claims description 10
- 230000009182 swimming Effects 0.000 claims description 9
- 238000010992 reflux Methods 0.000 claims 1
- 230000001954 sterilising effect Effects 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000006386 neutralization reaction Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- 206010015946 Eye irritation Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 231100000013 eye irritation Toxicity 0.000 description 1
- 230000007794 irritation Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012476 oxidizable substance Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案はプール内の水に最有効なオゾンを常時
確実に付与し、衛生的且つ健康的な環境状体を求
め得ようとする遊泳用プールの浄化装置に関する
ものである。[Detailed description of the invention] [Industrial application field] This invention is a swimming pool that always reliably provides the most effective ozone to the water in the pool and seeks a sanitary and healthy environment. This invention relates to a pool purification device.
近年、遊泳用プールの急速な利用に伴ない遊泳
客が増加し種々の施設改善が行なわれているが、
同時に水質の汚染度も問題となりその管理手段と
して薬材等の投入が挙げられている。
In recent years, with the rapid use of swimming pools, the number of swimmers has increased and various facility improvements have been made.
At the same time, the degree of water contamination has become a problem, and the introduction of medicinal materials has been cited as a means of managing it.
因みに温水プールの場合には水中の溶存酸素の
濃度が低いために該酸化力においては殆んど期待
することが困難であり、而も水中の被酸化物質は
残留塩素によつて主に酸化されているがために遊
泳者の員数の増加に伴つて当然、塩素注入量を増
加しなければならないが、この増加によつて目の
炎症は勿論のこと、刺激等の原因でもあつた。 Incidentally, in the case of a heated pool, it is difficult to expect much from the oxidizing power because the concentration of dissolved oxygen in the water is low, and the oxidizable substances in the water are mainly oxidized by residual chlorine. Therefore, as the number of swimmers increased, the amount of chlorine injected had to be increased, but this increase not only caused eye irritation but also caused irritation.
斯かる欠点を排除する手段として近時、水中の
次亜塩素によるトリハロメタンの生成による発ガ
ン性が問題であるがために塩素注入に代えオゾン
注入による強力な酸化力を利用しての殺菌浄化お
よび脱臭力が注目されプール水の過循環系列内
にオゾン発生装置を併設して槽水内にオゾンを注
入する方法が業界において種々開発されてきたの
である。 Recently, as a means to eliminate such drawbacks, since carcinogenicity due to the formation of trihalomethanes due to hypochlorite in water is a problem, sterilization and purification using the strong oxidizing power of ozone injection instead of chlorine injection has been proposed. The deodorizing power has attracted attention, and various methods have been developed in the industry for injecting ozone into the pool water by installing an ozone generator in the pool water overcirculation system.
即ち、その一例として第1図にて示す如く遊泳
用プール5のオーバーブロー水(汚染水)は上記
オーバーブロー側溝6よりオーバーブロー管6a
に流れ、此れが還水槽2にて一時貯水の後に還水
用配管B、エアーキヤツチヤー4、循環ポンプ
3、過器8、熱交換器9の回路を経て還水口ハ
よりプール5内に再たび還流されることゝなる。
また、底部吸込み口イよりの水(汚染水)は上記
配管Bの連結部ロに流れ、還水槽2よりの水と合
流して上記と同様の径路で還水する。 That is, as an example of this, as shown in FIG.
This water is temporarily stored in the return water tank 2, and then passes through the circuit of return water pipe B, air catcher 4, circulation pump 3, filter 8, and heat exchanger 9, and then enters the pool 5 from the return water port C. It will be refluxed again.
Further, the water (contaminated water) from the bottom suction port A flows to the connection part B of the pipe B, joins with the water from the water return tank 2, and is returned through the same route as above.
斯かる還水時においてオゾン発生装置1および
減菌装置10、凝集装置11、中和装置12の
夫々がプールの水質状況に応じて運転し槽内水の
浄化保持が行なわれていたのである。 During such water return, the ozone generator 1, sterilization device 10, flocculation device 11, and neutralization device 12 were operated according to the water quality of the pool to purify and maintain the water in the tank.
而るに上記、従来方法においては通常未反応の
余剰オゾンは過器8頂部8′或いは反応装置よ
り余剰オゾン送気管1aを通り活性炭等の処理装
置13に送られ吸収分解させて無臭化にし排気口
14より屋外に排出行なわれるのであるが電力コ
ストを用いて折角創出されたオゾンの一部を未反
応状体にて外部に廃棄することは非常に不経済で
あるは勿論のこと、更に上記無臭化用の活性炭の
使用交換に雑多な手数を要する等の欠点があつ
た。
However, in the above-mentioned conventional method, unreacted surplus ozone is normally sent from the top 8' of the filter 8 or the reaction device to the treatment device 13 for activated carbon, etc., through the surplus ozone supply pipe 1a, where it is absorbed and decomposed, deodorized, and then exhausted. Although it is discharged outdoors from the port 14, it is of course very uneconomical to dispose of a part of the ozone created at the cost of electricity to the outside in an unreacted state. There were drawbacks such as the need for various troubles to use and replace activated carbon for deodorization.
本考案は斯かる従来の不経済性の問題点に鑑み
て、その目的とするところは上記排オゾン処理装
置等を全く必要とすることなく通常排気されてい
た余剰オゾンを還水槽に送給行なわしめることに
よつて殺菌浄化機能の向上はもとより経済性効果
をも確実に期待しようとする遊泳用プールの浄化
装置を提供することにある。 In view of the uneconomical problem of the conventional method, the purpose of the present invention is to send surplus ozone that would normally be exhausted to a water return tank without the need for the above-mentioned exhaust ozone treatment equipment. It is an object of the present invention to provide a purifying device for a swimming pool that not only improves the sterilizing and purifying function but also reliably expects economical effects.
上記、目的を達成するために本考案の浄化装置
はオーバーブロー水の還水槽2と、循環ポンプ
3、過器8および熱交換器9等の機構装置を配
管Bにて各連結して過循環回路を形成すると共
に、該循環回路内にオゾン発生装置1を組込んで
なるプールの浄化装置において、上記過器8よ
り排出する未反応余剰オゾンを余剰オゾン送気管
Aを介して還水槽2に注入する排余剰オゾン還流
回路を併設せしめたことをその特徴としている。
In order to achieve the above object, the purification device of the present invention connects the overblown water return tank 2, circulation pump 3, filter 8, heat exchanger 9, etc. via piping B, and overcirculates the water. In a swimming pool purification device which forms a circuit and incorporates an ozone generator 1 into the circulation circuit, unreacted surplus ozone discharged from the filter 8 is sent to a return water tank 2 via a surplus ozone supply pipe A. Its feature is that it is also equipped with a recirculation circuit for injecting excess ozone.
本考案は上記の構成を有するものであつて、従
来の技術の項にて詳説した如くプール過循環運
転中において、過器8頂部排出口8′より排出
される余剰オゾンは、余剰オゾン送気管Aを経て
還水槽2内に噴出し槽内の比較的汚染濃度の高い
水質の一次殺菌を行なわしめる。
The present invention has the above-mentioned configuration, and as explained in detail in the section of the prior art, during pool overcirculation operation, surplus ozone discharged from the top discharge port 8' of the filter 8 is removed from the surplus ozone supply pipe. Through A, the water is ejected into the return tank 2 to perform primary sterilization of the water in the tank, which has a relatively high concentration of contaminants.
以下、本考案の実施例として温水用プールを第
2図に付いて詳説すると、符号2はプール5周辺
に設けられたオーバーブロー側溝6よりオーバー
ブロー管6aに流れるオーバーブロー水の還水
槽、3は該還水槽2の水を再度プール5内に還流
する機能を有した循環ポンプ、8は過器、9は
熱交換器で夫々が配管Bにて連結されている。
Hereinafter, a hot water pool will be described in detail with reference to FIG. 2 as an embodiment of the present invention. Reference numeral 2 denotes a return tank for overblown water flowing from an overblown gutter 6 provided around the pool 5 to an overblown pipe 6a; numeral 8 is a circulation pump having the function of returning the water from the water return tank 2 back into the pool 5; numeral 8 is a filter; and numeral 9 is a heat exchanger, which are connected to each other by piping B.
また他の符号4はヘヤーキヤチヤー、10は減
菌装置、11は凝集装置、12は中和装置、7は
補給水槽にて此れらの機構配列は従来と略同一系
列の構成を有している。 The other reference numerals 4 are a hair catcher, 10 is a sterilization device, 11 is a flocculation device, 12 is a neutralization device, and 7 is a replenishment water tank. .
本考案は叙上の構成においてオゾン発生装置1
を配管Bの過器8前方に連結設けると共に該
過器8頂部のオゾン排出口8′と上記還水槽2を
余剰オゾン送気管Aにて連結し、排余剰オゾンを
還水槽2内に噴出するように構成されている。 The present invention has an ozone generator 1 in the above configuration.
is connected to the front of the filter device 8 in the pipe B, and the ozone discharge port 8' at the top of the filter device 8 is connected to the above-mentioned return water tank 2 by the surplus ozone air supply pipe A, and the exhausted surplus ozone is spouted into the return water tank 2. It is configured as follows.
なお上記還水槽2の容積は、プールにおける多
人数の人水や飛び込み時の増量を受けるために充
分な容積を有するもので、此れが故に未反応余剰
オゾンの反応が充分に作用し、且つ余剰オゾン送
気管Aには循環ポンプによる背圧力が存在してい
るがために還水槽2内に注入された余剰オゾンの
噴出により自然的に撹拌されてより有効な酸化が
実行されて吸収効果を向上させていることは謂う
までもない。 The volume of the return water tank 2 is sufficient to accommodate the increased amount of water used by a large number of people in the pool or when people jump into the pool, so that the reaction of unreacted excess ozone can take place sufficiently. Since back pressure from the circulation pump exists in the surplus ozone air supply pipe A, the surplus ozone injected into the water return tank 2 is naturally agitated by the ejection and more effective oxidation is carried out, increasing the absorption effect. Needless to say, it has improved.
従つて該排余剰オゾンをして還水槽2内に流入
せる汚水の一次殺菌浄化が確実良好に行なわれ、
上記オゾンの注入、減菌装置10、中和装置等に
よる浄化作用と併せて法定基準に適合せる有効な
プール水を確実容易に供用することができ得るの
である。 Therefore, the primary sterilization and purification of the wastewater, which is caused by the discharged surplus ozone and flows into the return water tank 2, is carried out reliably and satisfactorily.
In combination with the purifying action of the ozone injection, sterilization device 10, neutralization device, etc., it is possible to reliably and easily provide effective pool water that meets legal standards.
以上の如く本考案に係る遊泳用プールの浄化装
置は従来外部に排気されていた未反応余剰オゾン
を全く廃棄することなく汚染度の高い還水槽2内
に注入行なわしめることによつてオゾンの使用全
量を大巾に抑制でき得るは勿論活性炭等による排
オゾン処理装置、排気設備等をも全く必要とする
ことなく此れらに伴う労力的、経済的効果が頗ぶ
る大である。
As described above, the swimming pool purification device according to the present invention utilizes ozone by injecting the unreacted surplus ozone, which was conventionally exhausted outside, into the highly contaminated return water tank 2 without disposing of it at all. Not only can the total amount be greatly suppressed, but there is no need for exhaust ozone treatment equipment using activated carbon or the like, exhaust equipment, etc., and the labor and economic effects associated with these are enormous.
なお、本考案は遊泳用プールのみに限定される
ものではなく浴槽、水槽等他の槽具にも汎く利用
でき得ることは勿論である。 It goes without saying that the present invention is not limited to only swimming pools, but can be widely used for other bath equipment such as bathtubs and aquariums.
第1図は従来、開発されているプールの浄化装
置の略解図。第2図は本考案に係る遊泳用プール
の浄化装置の全体略解図である。
符号の説明、1……オゾン発生装置、2……還
水槽、8……過器、A……余剰オゾン送気管、
B……還水用配管。
FIG. 1 is a schematic diagram of a conventional pool purification device. FIG. 2 is an overall schematic diagram of the swimming pool purification device according to the present invention. Explanation of symbols, 1... Ozone generator, 2... Return water tank, 8... Passage device, A... Excess ozone air pipe,
B...Return water piping.
Claims (1)
3、過器8および熱交換器9等の機構装置を配
管Bにて各連結して過循環回路を形成すると共
に該循環回路内にオゾン発生装置1を組込んでな
るプールの浄化装置において、上記過器8より
排出する未反応余剰オゾンを余剰オゾン送気管A
を介して還水槽2に注入する排余剰オゾン還流回
路を併設せしめたことを特徴とする遊泳用プール
の浄化装置。 The overblown water return tank 2 and mechanical devices such as the circulation pump 3, the filter 8, and the heat exchanger 9 are connected via piping B to form an overcirculation circuit, and an ozone generator 1 is installed in the circulation circuit. In a swimming pool purification device incorporating a
A purification device for a swimming pool, characterized in that it is also equipped with a recirculation circuit for injecting surplus ozone into a recirculation tank 2 via a reflux circuit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15780588U JPH0323358Y2 (en) | 1988-12-02 | 1988-12-02 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15780588U JPH0323358Y2 (en) | 1988-12-02 | 1988-12-02 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0281697U JPH0281697U (en) | 1990-06-25 |
| JPH0323358Y2 true JPH0323358Y2 (en) | 1991-05-21 |
Family
ID=31437569
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15780588U Expired JPH0323358Y2 (en) | 1988-12-02 | 1988-12-02 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0323358Y2 (en) |
-
1988
- 1988-12-02 JP JP15780588U patent/JPH0323358Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0281697U (en) | 1990-06-25 |
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