JP2530768Y2 - Water purification equipment - Google Patents

Water purification equipment

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Publication number
JP2530768Y2
JP2530768Y2 JP1991025402U JP2540291U JP2530768Y2 JP 2530768 Y2 JP2530768 Y2 JP 2530768Y2 JP 1991025402 U JP1991025402 U JP 1991025402U JP 2540291 U JP2540291 U JP 2540291U JP 2530768 Y2 JP2530768 Y2 JP 2530768Y2
Authority
JP
Japan
Prior art keywords
ozone
water
reaction chamber
space
catalyst
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
JP1991025402U
Other languages
Japanese (ja)
Other versions
JPH04114493U (en
Inventor
剛 牧野
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.)
Toyota Auto Body Co Ltd
Original Assignee
Toyota Auto Body Co 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 Toyota Auto Body Co Ltd filed Critical Toyota Auto Body Co Ltd
Priority to JP1991025402U priority Critical patent/JP2530768Y2/en
Publication of JPH04114493U publication Critical patent/JPH04114493U/en
Application granted granted Critical
Publication of JP2530768Y2 publication Critical patent/JP2530768Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案はオゾンを利用して水を浄
化する浄水装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purification device for purifying water using ozone.

【0002】[0002]

【従来の技術】水槽の水等を、オゾンで殺菌したり浄化
したりする従来の方法は、図3に示すようにポンプaに
より水槽bの水をオゾン溶解水槽cへ導き、オゾン発生
器dで発生したオゾンをエアコンプレッサeにより送風
される加圧空気とともに、前記オゾン溶解水槽cに導い
て散気管fから噴出させてバブリングし溶解させること
により行ってきた。また、特開昭52−7874号公報
には、触媒層の上方から流下させる処理水に対して直交
するように、オゾンを触媒層に流過させるようにして浄
水する気液接触装置が開示されている。
2. Description of the Related Art A conventional method for sterilizing or purifying water in a water tank with ozone is as follows. As shown in FIG. 3, a pump a guides water in a water tank b to an ozone-dissolving water tank c, and an ozone generator d. The ozone generated in step (1) is led to the above-mentioned ozone dissolving water tank c together with the pressurized air blown by the air compressor e, and ejected from the diffuser f to bubble and dissolve. Also, JP-A-52-7874
Is perpendicular to the treated water flowing down from above the catalyst layer.
Ozone is passed through the catalyst layer to purify
A water-gas contact device is disclosed.

【0003】[0003]

【考案が解決しようとする課題】しかしながら、図3に
示す方法により、オゾンの水中での溶解効率を高めるた
めには、オゾンと水の接触時間を長くするために、水深
の深い大型のオゾン溶解水槽が必要となる。また、オゾ
ンが溶解した浄化後の水をそのまま水槽bに戻すと、水
槽bのオゾン濃度が高まり生物やゴム等のシール部材に
危害をあたえる虞れがある。このため、水中のオゾンを
分解するオゾン分解触媒gを備える必要がある。その
他、水中に溶解しないで排出されるオゾンを分解して外
気へ放出するためのオゾン分解触媒hも必要となり、装
置全体が大型化するという問題点がある。さらに、上記
方法では、水中に溶解するオゾンの割合は40〜70%
と低く効率が悪いという問題点もある。また、特開昭5
2−7874号公報に示された気液接触装置は、オゾン
を処理水の流向に対して直交するように流過させるた
め、触媒層を各層に区画するとともに、各区画の互い違
いの端部にフィルタを設けるとともに、オゾン流入通路
を形成する必要があり構成が複雑となる。本考案は、上
記問題点を解決するためになされたもので、浄化効率が
高く装置の小型化が可能な浄水装置を提供することを目
的とするものである。
[Problem to be solved by the invention] However, FIG.
According to the method shown , in order to increase the dissolving efficiency of ozone in water, a large ozone dissolving water tank having a deep water depth is required to prolong the contact time of ozone and water. Further, if the purified water in which ozone is dissolved is returned to the water tank b as it is, the ozone concentration in the water tank b increases, and there is a possibility that the sealing member such as a living thing or rubber may be harmed. Therefore, it is necessary to provide an ozone decomposition catalyst g for decomposing ozone in water. In addition, an ozone decomposing catalyst h for decomposing ozone discharged without dissolving in water and releasing the ozone to the outside air is required, and there is a problem that the entire apparatus becomes large. Further, in the above method, the ratio of ozone dissolved in water is 40 to 70%.
And the efficiency is low. In addition, Japanese Unexamined Patent Publication
The gas-liquid contact device disclosed in Japanese Patent Publication No.
Flow through the treated water at right angles to the flow direction of the treated water.
For this reason, partition the catalyst layer into layers, and
A filter is provided at the other end and an ozone inflow passage
Must be formed, and the configuration becomes complicated. The present invention has been made to solve the above problems, and an object of the present invention is to provide a water purification device that has high purification efficiency and can reduce the size of the device.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
の具体的手段として、底部に開口を設けたオゾン反応室
と、該オゾン反応室の前記底部開口を塞ぐとともに、オ
ゾン反応室内の上部に空間を形成するように配置された
通気性のオゾン分解触媒と、前記空間内に浄化すべき水
を散水するために配設したスプレーノズルと、前記空間
内にオゾンを供給するオゾン供給手段とを具備したこと
を特徴とする浄水装置が提供される。
As specific means for achieving the above object, according to the solution to ## and the ozone reaction chamber having an opening at the bottom, with closing the bottom opening of the ozone reaction chamber, O
A gas-permeable ozonolysis catalyst arranged to form a space in the upper part of the reaction chamber, and water to be purified in the space.
A spray nozzle arranged to spray water and the space
And an ozone supply means for supplying ozone therein.

【0005】[0005]

【作用】上記浄水装置の作用は以下の通りである。オゾ
ン供給手段によりオゾン反応室の上部の空間に供給され
たオゾンは、該空間内にスプレーノズルから細かい水滴
状となって散水された浄化すべき水と混合する。混合水
中のオゾンは通気性のオゾン分解触媒を通過する際に分
解され発生期の酸素を生じ、オゾン分解触媒中を流下す
る水を浄水する。分解されて酸素となったオゾンは、オ
ゾン反応室から大気中に排気される。
[Operation] The operation of the above-mentioned water purification device is as follows. The ozone supplied to the space above the ozone reaction chamber by the ozone supply means contains fine water droplets from the spray nozzle in the space.
And mixed with the water to be purified which has been sprinkled. Mixed water
Ozone Ji oxygen decomposed nascent raw when passing through the breathable ozonolysis catalyst in, to flow down the ozone decomposing catalyst
Water. Ozone decomposed into oxygen is exhausted from the ozone reaction chamber to the atmosphere.

【0006】[0006]

【実施例】本考案の実施例を添付図面を参照して説明す
る。図1は本考案の浄水装置Aを用いて水槽の水を殺菌
浄化するシステムの概略構成図である。浄水装置Aは、
オゾン発生器1、オゾン反応室2、オゾン分解触媒3、
エアーコンプレッサ4及びスプレーノズル5等から構成
される。オゾン反応室2は底部を開放して開口2aを設
け、その開口2aを塞ぐようにオゾン分解触媒3が配置
されている。オゾン分解触媒3は金属酸化物例えば二酸
化マンガンや二酸化ケイ素等を通気性を確保して充填し
たものや、活性炭を利用したものを用いる。オゾン反応
室2には、オゾン分解触媒3の上部に空間2bが形成さ
れ、該空間2b内にスプレーノズル5を配設する。そし
て、天井中心部にオゾン流入管6を連結してオゾン発生
器1に接続する。エアーコンプレッサ4はオゾン発生器
1の前段に配置する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described with reference to the accompanying drawings. FIG. 1 is a schematic configuration diagram of a system for sterilizing and purifying water in a water tank using the water purification device A of the present invention. Water purification device A
Ozone generator 1, ozone reaction chamber 2, ozone decomposition catalyst 3,
It comprises an air compressor 4 and a spray nozzle 5 and the like. The ozone reaction chamber 2 is provided with an opening 2a with an open bottom, and an ozone decomposition catalyst 3 is arranged so as to close the opening 2a. As the ozone decomposition catalyst 3, a catalyst filled with a metal oxide such as manganese dioxide or silicon dioxide while ensuring air permeability, or a catalyst utilizing activated carbon is used. Ozone reaction
In the chamber 2, a space 2b is formed above the ozone decomposition catalyst 3.
Then, the spray nozzle 5 is disposed in the space 2b . Soshi
Then , the ozone inflow pipe 6 is connected to the center of the ceiling and connected to the ozone generator 1. The air compressor 4 is arranged before the ozone generator 1.

【0007】水槽7の下方側部には吸水管8を挿通配置
し、該吸水管8にストレーナ9を連結してポンプ10に
接続する。該ポンプ10の吐出口と前記スプレーノズル
5とを配管11により接続する。
A water absorption pipe 8 is inserted through the lower side of the water tank 7, and a strainer 9 is connected to the water absorption pipe 8 and connected to a pump 10. The discharge port of the pump 10 and the spray nozzle 5 are connected by a pipe 11.

【0008】上記構成の殺菌浄化システムの作動を以下
に説明する。オゾン発生器1で発生したオゾンは、エア
ーコンプレッサ4からの加圧空気と混合されてオゾン流
入管6を通ってオゾン反応室2の空間2b内へ送給され
る。一方、水槽7の水はポンプ10により吸水管8を通
って吸水され、ストレーナ9により浮遊する大きなゴミ
等を取り除いた後配管11に吐出され、スプレーノズル
5から細かい水滴となってオゾン反応室2の空間2b
に散水される。
The operation of the sterilizing and purifying system having the above configuration will be described below. The ozone generated by the ozone generator 1 is mixed with the pressurized air from the air compressor 4 and sent through the ozone inflow pipe 6 into the space 2b of the ozone reaction chamber 2. On the other hand, the water in the water tank 7 is absorbed by a pump 10 through a water absorption pipe 8, and is discharged to a pipe 11 after removing large floating dust and the like by a strainer 9. Is sprayed in the space 2b .

【0009】オゾン反応室2の空間2bへ送給されたオ
ゾンと加圧空気の混合気体は、スプレーノズル5から散
水される細かい水滴と混ざりあって、オゾン分解触媒3
中を通過する。このときオゾンは、分解されてO→O
+O・の化学変化を生じ酸化力の大変強力な発生期の
酸素「O・」が発生する。オゾン分解触媒3中を流下す
る水に含まれる有機物や微生物は、前記発生期の酸素
「O・」により酸化浄化されたり殺菌される。オゾン分
解触媒3を通過した水はオゾン反応室2の底部の開口2
aからシャワー状になって水槽7に落下する。そして、
オゾンが分解された酸素を含む加圧空気も、前記開口2
aから排気される(図2参照)。
The mixed gas of ozone and pressurized air supplied to the space 2b of the ozone reaction chamber 2 mixes with fine water droplets sprayed from the spray nozzle 5, and the ozone decomposition catalyst 3
Pass through. At this time, the ozone is decomposed to O 3 → O
A chemical change of 2 + O. Is generated, and very strong nascent oxygen "O." of oxidizing power is generated. Organic substances and microorganisms contained in the water flowing down in the ozone decomposition catalyst 3 are oxidized and purified or sterilized by the above-mentioned oxygen "O." The water passing through the ozonolysis catalyst 3 is supplied to the opening 2 at the bottom of the ozone reaction chamber 2.
a into a water tank 7 in the form of a shower. And
Pressurized air containing oxygen in which ozone is decomposed is also present in the opening 2
The gas is exhausted from a (see FIG. 2).

【0010】上記オゾン分解触媒3として、二酸化マン
ガンや二酸化ケイ素等の金属酸化物若しくは活性炭を利
用した触媒を用いているから、オゾン分解効率が約90
%と高い。このため、発生期の酸素「O・」による酸化
力も殺菌力も強力となり浄水効率も高くなる。
As the ozone decomposing catalyst 3, a catalyst using a metal oxide such as manganese dioxide or silicon dioxide or activated carbon is used, so that the ozone decomposing efficiency is about 90%.
% And high. For this reason, the oxidizing power and the bactericidal power by the oxygen “O •” in the nascent period are strong, and the water purification efficiency is also increased.

【0011】[0011]

【考案の効果】本考案は上記した構成を有し、オゾン反
応室内の上部に形成した空間内にオゾンを供給するとと
もに、浄化すべき水をスプレーノズルで散水させ、予め
オゾンと水とが混合した気液接触状態を形成してオゾン
分解触媒中を通過させ、オゾン分解触媒で分解されて発
生する発生期の酸素により浄水するものであるから、
生期の酸素に接触する割合が高まり浄水効率が向上す
る。また、オゾン溶解用の水深の深い大型水槽や、水槽
への還流水に溶解するオゾンを分解するためのオゾン分
解触媒や、水中に溶解しないで排出されるオゾンを分解
して外気へ放出するためのオゾン分解触媒も不必要とな
るばかりでなく、触媒層を各層に区画するとともに、各
区画の互い違いの端部にフィルタを設けるとともに、オ
ゾン流入通路を形成する必要がないから、装置全体を簡
易小型化することができる等の優れた効果がある。
[Effect of the invention] The present invention has a configuration described above, supplies the ozone into the space formed in the upper portion of the ozone reaction chamber, the to be purified water was sprinkled with a spray nozzle, in advance
Ozone and to form a gas-liquid contact state of mixture of the water passed through the ozone decomposition catalyst, since it is intended to clean water by nascent oxygen generated is decomposed by the ozone decomposition catalyst, issued
The rate of contact with oxygen during the growing period increases, and water purification efficiency improves.
You. Also, a large deep water tank for dissolving ozone, an ozone decomposition catalyst for decomposing ozone dissolved in reflux water to the water tank, and decomposing ozone discharged without dissolving in water and releasing it to the outside air Ozone decomposition catalyst is unnecessary
In addition to partitioning the catalyst layer into layers,
Provide filters at alternating ends of the compartment and
Since there is no need to form a zonal inflow passage, there is an excellent effect that the entire apparatus can be simplified and miniaturized.

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

【図1】本考案の浄水装置を用いた殺菌浄化システムの
概略構成図である。
FIG. 1 is a schematic configuration diagram of a sterilization and purification system using the water purification device of the present invention.

【図2】オゾン反応室の拡大断面図である。FIG. 2 is an enlarged sectional view of an ozone reaction chamber.

【図3】従来の殺菌浄化システムの概略構成図である。FIG. 3 is a schematic configuration diagram of a conventional sterilization and purification system.

【符号の説明】[Explanation of symbols]

1...オゾン発生器、 2...オゾン反応室、 2
a...開口、 2b...空間、 3...オゾン分
解触媒、 5...スプレーノズル、 7...水槽、
A...浄水装置。
1. . . Ozone generator, 2. . . Ozone reaction chamber, 2
a. . . Opening, 2b. . . Space , 3. . . Ozone decomposition catalyst, 5. . . Spray nozzle, 7. . . Aquarium,
A. . . Water purification equipment.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 550 C02F 1/50 550B 560 560Z ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical indication location C02F 1/50 550 C02F 1/50 550B 560 560Z

Claims (1)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 底部に開口を設けたオゾン反応室と、該
オゾン反応室の前記底部開口を塞ぐとともに、オゾン反
応室内の上部に空間を形成するように配置された通気性
のオゾン分解触媒と、前記空間内に浄化すべき水を散水
するために配設したスプレーノズルと、前記空間内に
ゾンを供給するオゾン供給手段とを具備したことを特徴
とする浄水装置。
1. A ozone reaction chamber having an opening at the bottom, with closing the bottom opening of the ozone reaction chamber, ozone reaction
A gas-permeable ozonolysis catalyst arranged so as to form a space in the upper part of the reaction chamber, and water to be purified in the space
A water purification device , comprising: a spray nozzle provided to perform the cleaning; and ozone supply means for supplying ozone into the space .
JP1991025402U 1991-03-22 1991-03-22 Water purification equipment Expired - Lifetime JP2530768Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991025402U JP2530768Y2 (en) 1991-03-22 1991-03-22 Water purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991025402U JP2530768Y2 (en) 1991-03-22 1991-03-22 Water purification equipment

Publications (2)

Publication Number Publication Date
JPH04114493U JPH04114493U (en) 1992-10-08
JP2530768Y2 true JP2530768Y2 (en) 1997-03-26

Family

ID=31910144

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991025402U Expired - Lifetime JP2530768Y2 (en) 1991-03-22 1991-03-22 Water purification equipment

Country Status (1)

Country Link
JP (1) JP2530768Y2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS527874A (en) * 1975-07-09 1977-01-21 Toshiba Mach Co Ltd Gas-liquid contact apparatus

Also Published As

Publication number Publication date
JPH04114493U (en) 1992-10-08

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Effective date: 19961029