JPH0645030B2 - Ozone water treatment equipment - Google Patents

Ozone water treatment equipment

Info

Publication number
JPH0645030B2
JPH0645030B2 JP62050812A JP5081287A JPH0645030B2 JP H0645030 B2 JPH0645030 B2 JP H0645030B2 JP 62050812 A JP62050812 A JP 62050812A JP 5081287 A JP5081287 A JP 5081287A JP H0645030 B2 JPH0645030 B2 JP H0645030B2
Authority
JP
Japan
Prior art keywords
water
ozone
filter
raw water
filter medium
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 - Fee Related
Application number
JP62050812A
Other languages
Japanese (ja)
Other versions
JPS63166494A (en
Inventor
利彦 佐々木
初男 四元
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP62050812A priority Critical patent/JPH0645030B2/en
Publication of JPS63166494A publication Critical patent/JPS63166494A/en
Publication of JPH0645030B2 publication Critical patent/JPH0645030B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は水質改善、およびろ過装置洗浄にオゾンを注
入し、原水の水質改善、ろ過装置の洗浄を高効率でしか
も経済的に行うものに関するものである。
Description: [Industrial field of application] The present invention relates to a method for improving water quality, injecting ozone into cleaning of a filtering device, improving the water quality of raw water, and cleaning the filtering device with high efficiency and economically. It is a thing.

〔従来の技術〕[Conventional technology]

第2図は従来の浴場における配管系統を示すフロー図で
あり、図において、(1)は浴場水、(2)は循環水量調整
弁、(3)は集毛器、(4)は原水ポンプ、(5)は正循環弁、
(6)は逆洗弁、(7)は逆洗排水弁、(8)はろ過装置、(9)は
空気抜弁で、ろ過装置(8)内にたまった空気を自動的に
排出する。(10)は浴場返送弁、(11)は熱交換各で浴場水
の温度を一定に保つ、(12)は次亜塩素酸タンク、(13)は
次亜塩素酸ソーダ注入ポンプ、(14)は高分子凝集剤タン
ク、(15)は高分子凝集剤注入ポンプ、(16)は固形塩素投
入タンク、(17)は逆洗水供給水管、(18)は給水弁、(19)
は逆洗水貯留タンク、(20)は逆洗供給弁である。
Fig. 2 is a flow chart showing a piping system in a conventional bathhouse. In the figure, (1) is bath water, (2) is a circulating water amount adjusting valve, (3) is a hair collector, and (4) is a raw water pump. , (5) is a positive circulation valve,
(6) is a backwash valve, (7) is a backwash drain valve, (8) is a filtration device, and (9) is an air vent valve, which automatically discharges the air accumulated in the filtration device (8). (10) is a bath return valve, (11) keeps the bath water temperature constant at each heat exchange, (12) is a hypochlorous acid tank, (13) is a sodium hypochlorite injection pump, (14) Is a polymer coagulant tank, (15) is a polymer coagulant injection pump, (16) is a solid chlorine feed tank, (17) is a backwash water supply pipe, (18) is a water supply valve, (19)
Is a backwash water storage tank, and (20) is a backwash supply valve.

次に動作について説明する。浴場水(1)は矢印Aの循環
系により清浄化される。つまり、弁(2),(5),(10)が開
放、弁(6),(7),(20)が閉、原水ポンプ(4),薬品注入
ポンプ(13),(14)は運転状態である。従って浴場水(1)
は、次亜塩素酸ソーダ(12),高分子凝集剤(14)が注入さ
れ、次亜塩素酸による殺菌,高分子凝集剤により、浴場
水の微細な汚濁物質を粗大フロック化させる。薬剤(1
2),(13)を注入された浴場水(1)は集毛器(3)で浴場水
(1)に混入した毛髪が除去され、原水ポンプ(4)により循
環送水される。原水ポンプ(4)により送水された浴場水
(1)は、汚濁度が高い場合は更に、固形塩素投入タンク
(16)より固形塩素が投入され浴場水(1)に混入され、薬
剤が増量される前述の薬剤により殺菌,粗大フロック化
された浴場水(1)はろ過装置(8)の上部より入り、ろ過装
置(8)のろ材により粗大フロック化された汚濁物質は、
ろ材に捕捉される。ろ過装置(8)内に一部混入した空気
は、一定量の空気量になると空気抜き弁(9)により自動
排出される。ついで、ろ過装置(8)により汚濁物質を除
去された浴場水(1)は浴場返送弁(10)を経由し、熱交換
器(11)により適温に加温され浴場に送水される。
Next, the operation will be described. The bath water (1) is cleaned by the circulation system indicated by arrow A. That is, valves (2), (5), (10) are open, valves (6), (7), (20) are closed, raw water pump (4), chemical injection pumps (13), (14) are in operation. It is in a state. Therefore bath water (1)
Sodium hypochlorite (12) and polymer flocculant (14) are injected, and sterilization with hypochlorous acid causes the macroscopic flocculation of fine pollutants in bath water by the polymer flocculant. Drug (1
Bath water (1) injected with 2) and (13) is bath water with the hair collector (3).
Hair mixed in (1) is removed, and water is circulated by the raw water pump (4). Bath water sent by the raw water pump (4)
(1) is a solid chlorine input tank when the pollution level is high.
Solid chlorine is added from (16) and mixed into the bath water (1) to increase the amount of the drug. The bath water (1) sterilized and coarsely flocculated by the above-mentioned drug enters from the upper part of the filter (8) The pollutants coarsely flocculated by the filter medium of the filtration device (8) are
It is captured by the filter medium. The air partially mixed in the filtering device (8) is automatically discharged by the air vent valve (9) when a certain amount of air is reached. Next, the bath water (1) from which contaminants have been removed by the filtration device (8) passes through the bath return valve (10), is heated to an appropriate temperature by the heat exchanger (11), and is sent to the bath.

次にろ過装置(8)のろ材の許容量の汚濁物質を捕捉する
と、ろ過装置の効果がなくなるので、この段階で捕捉し
た汚濁物質を系外へ排出しなければならない、つまりろ
過装置に矢印Bの系統の逆洗洗浄が必要であるためこの
例について説明する。
Next, if the permissible amount of contaminants of the filter medium of the filter (8) is captured, the effect of the filter is lost, so the contaminant captured at this stage must be discharged to the outside of the system, that is, the arrow B indicates to the filter. This example will be described because the backwashing and cleaning of the system of (1) is required.

例えば水道水が逆洗水供給管(17)に接続され、給水弁(1
8)を開して逆洗水貯留タンク(19)に貯水される。逆洗時
の系統弁の状態は弁(20),(6),(7)が開、弁(2),(5),
(10)は閉,原水ポンプ(4)は運転,薬剤ポンプ(13),(1
5)は停止状態である。つまり逆洗貯留タンクの水は、逆
洗弁(20)を通り原水ポンプ(4)により弁(6)を通り、ろ過
装置(8)の下部から上方へ吹き上げ、ろ過装置(8)内のろ
材に捕捉した汚濁物質を逆洗水により押し出し、弁(7)
を経由して系外にドレンとして排出する。
For example, tap water is connected to the backwash water supply pipe (17) and the water supply valve (1
8) is opened and water is stored in the backwash water storage tank (19). The state of the system valve at the time of backwash is such that valves (20), (6), (7) are open, and valves (2), (5),
(10) is closed, raw water pump (4) is in operation, chemical pump (13), (1
5) is in a stopped state. That is, the water in the backwash storage tank passes through the backwash valve (20), the raw water pump (4), the valve (6), and is blown upward from the lower part of the filtration device (8). The contaminants captured on the valve were pushed out by backwashing water, and the valve (7)
It is discharged as drain through the system.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

従来のろ過装置を有し、循環使用する例えば浴場の水処
理装置は以上のように構成されているので、薬剤である
例えば次亜塩素酸ソーダ,高分子凝集剤,又高汚濁時の
薬剤増量のための固形塩素剤が、多量必要とするため浴
場において例えば塩素臭が濃く、人に不快感を与えるば
かりでなく金属を腐食させ、植物を枯れさせていた、
又、高分子凝集剤により過大に粗大フロック化するた
め、これがろ過装置のろ材表面を早期に塞ぐため、多回
数の逆洗が必要であり、又一般にはろ過装置のろ材とし
て小径の砂質のものが積層して構成されるため、微生物
が繁殖するのが常で、この微生物がろ材内に増殖すると
例えば水道水による逆水洗浄のみでは、完全に除去でき
ないためろ材が回復できず、まれには流出し浴場に送水
されるなどの問題があった。
Since the conventional water treatment device for circulating water, which has a conventional filtering device, is configured as described above, it is necessary to increase the amount of chemicals such as sodium hypochlorite, polymer flocculant, and chemicals when highly polluted. The solid chlorine agent for requires a large amount, for example, has a strong chlorine odor in the bath, which not only makes people uncomfortable but also corrodes metals and kills plants.
In addition, the polymer flocculant causes excessive coarse flocculation, which blocks the filter medium surface of the filtration device at an early stage, and therefore requires backwashing many times. Since it is composed by stacking things, microorganisms usually propagate, and if this microorganism grows in the filter medium, for example, it cannot be completely removed by only backwashing with tap water, so the filter medium cannot be recovered, and in rare cases There was a problem that the water leaked and was sent to the bathhouse.

この発明は、上記のような問題点を解消するためになさ
れたもので、薬剤の大巾な減量もしくは不要化し、ろ材
内に繁殖した微生物を除去し、ろ過装置の逆洗回数もし
くは逆洗水量を大巾に低減し、ろ材の完全な回復を計る
とともに、水質,雰囲気を大巾に改善できる水処理装置
を得ることを目的とする。
This invention has been made in order to solve the above problems, a large reduction or elimination of the need for chemicals, remove the microorganisms that have propagated in the filter medium, the backwashing frequency of the filtration device or the amount of backwashing water. The purpose of the present invention is to obtain a water treatment device that can significantly reduce the water content, measure the complete recovery of the filter medium, and greatly improve the water quality and atmosphere.

〔問題点を解決するための手段〕[Means for solving problems]

この発明に係るオゾン処理装置は、原水にオゾンを高効
率に反応吸収させ水質改善を計るとともに薬剤の大巾な
低減あるいは不使用化し、さらにろ過装置のろ材逆洗に
オゾン水と微細なオゾン化ガスによりろ材内部に発生し
た微生物、および捕捉した汚濁物質を効率よく除去でき
るようにしたものである。
The ozone treatment apparatus according to the present invention efficiently reacts and absorbs ozone in raw water to improve the water quality, greatly reduces or eliminates the use of chemicals, and further uses ozone water and fine ozone to backwash the filter medium of the filter. The gas is capable of efficiently removing the microorganisms generated inside the filter medium and the trapped pollutants.

〔作用〕[Action]

この発明における水質改善のためのオゾン水処理装置は
原水あるいは洗浄水の一部を分岐し、その分岐回路にエ
ジェクターを配備し、オゾンを作るとともに微細なオゾ
ン化ガス量を原水ポンプのキャビテーションを起こさな
い量のオゾン化ガス量に抑え、ポンプエンペラーの攪拌
によるオゾン吸収率を向上させるとともに、ろ過装置の
ろ材逆洗時には、ろ材内部にオゾン水と、微細な未反応
オゾン化ガスを吹き込み、ろ材内部に発生した微生物を
殺すとともに、微細なオゾン化ガスの浮上力によりろ材
層間の汚濁物質を系外へ除去でき、ろ材の清浄化が効率
的にすることができる。
The ozone water treatment device for improving water quality in this invention branches a part of raw water or wash water, and arranges an ejector in the branch circuit to make ozone and generate a fine amount of ozonized gas to cause cavitation of a raw water pump. It suppresses the amount of ozonized gas that does not exist, improves the ozone absorption rate by stirring the pump Emperor, and blows ozone water and fine unreacted ozonized gas into the filter medium when backwashing the filter medium of the filtration device. It is possible to kill the microorganisms generated at the same time and remove the contaminants between the layers of the filter medium to the outside of the system by the floating force of the fine ozonized gas, so that the filter medium can be efficiently cleaned.

〔発明の実施例〕Example of Invention

以下、この発明の一実施例を図について説明する。第1
図において(21)は循環水分岐弁、(22)は逆洗水分岐弁、
(23)はエジェクターで、水に流速をもって通水すると吸
引ガスを微細気泡化混合させる。(24)は分岐水返送弁で
原水ポンプ(4)の吸引側の主管に混合される。(25)はオ
ゾン発生装置で空気あるいは酸素からオゾンを生成す
る。(26)はオゾン供給弁,(27)はチャッキ弁でオゾン発
生器への水の逆流を防止する様配備される。
An embodiment of the present invention will be described below with reference to the drawings. First
In the figure, (21) is a circulating water branch valve, (22) is a backwash water branch valve,
(23) is an ejector, which sucks gas into fine air bubbles and mixes when water is passed through at a flow rate. (24) is a branch water return valve, which is mixed with the main pipe on the suction side of the raw water pump (4). (25) is an ozone generator that generates ozone from air or oxygen. (26) is an ozone supply valve, and (27) is a check valve, which is arranged to prevent backflow of water to the ozone generator.

次に動作について説明する。浴場水(1)は矢印Aの循環
系により清浄化される。つまり弁(2),(5),(10),(2
1),(24),(26)が開,原水ポンプ(4)、オゾン発生装置
(25)が運転状態、つまり浴場水(1)は、弁(2),集毛器
(3),原水ポンプ(4),弁(5),ろ過装置(8),を通り弁(1
0)から熱交換器(11)で加温されて浴場へ返送されるが、
オゾン水濃度を高めるため清浄水化されたろ過装置を経
たろ過水を、設定量分岐し弁(21)を経てエジェクター(2
3),弁(24)を通り、前述の浴場水(1)の循環水と原水ポ
ンプ(4)の吸引側で混合される。
Next, the operation will be described. The bath water (1) is cleaned by the circulation system indicated by arrow A. That is, valves (2), (5), (10), (2
1), (24), (26) open, raw water pump (4), ozone generator
(25) is in operating condition, that is, bath water (1) is valve (2), hair collector
(3), raw water pump (4), valve (5), filtration device (8), through valve (1
It is heated by the heat exchanger (11) from 0) and returned to the bath,
In order to increase the concentration of ozone water, the filtered water that has passed through the filter device that has been purified water is branched into a set amount and passed through the valve (21) to the ejector (2
3), through the valve (24), the circulating water of the bath water (1) and the suction side of the raw water pump (4) are mixed.

このときエジェクター(23)の吸引部にはオゾン発生器(2
5)により発生したオゾン化ガスが、弁(26),チャッキ弁
(27)を経てエジェクター(23)に吸引注入され、ここでオ
ゾン化ガスは微細気泡化され、分岐水と混合することに
より、分岐水と次亜塩素酸ソーダの数倍から数千倍の酸
化力を持つと言われるオゾンにより殺菌,有機物の分解
等により水質改善処理が行なわれると共に、一部はオゾ
ン水又、一部の未反応オゾン化ガスは、微細化気泡のま
ま原水ポンプ(4)の吸引側で混合され、更に原水ポンプ
(4)内で原水ポンプエンペラーにより混合は促進され、
分岐水のオゾン水、微細なオゾン化ガスは、循環水全量
に高効率に反応吸収される。従って、このことにより循
環水全量はオゾンにより高品位の水質に改善され、ろ過
装置(8)に入り、浮遊物質はろ材層に捕捉され、オゾン
により殺菌,脱色,脱臭を含む水質改善されて清浄な水
となって、浴場へ返送される。
At this time, the ozone generator (2
The ozonized gas generated by 5) is the valve (26) and the check valve.
After being injected into the ejector (23) via (27), the ozonized gas is made into fine bubbles and mixed with the branched water to oxidize the branched water and sodium hypochlorite several times to several thousand times. It is said that ozone, which is said to have power, is used to sterilize water and to improve water quality by decomposing organic matter, etc., and part of the ozone water and some unreacted ozonized gas remain in the form of atomized bubbles in the raw water pump (4). Is mixed on the suction side of
In (4), mixing is promoted by the raw water pump emperor,
The ozonized water and fine ozonized gas of the branched water are highly efficiently reacted and absorbed by the total amount of circulating water. Therefore, by this, the total amount of circulating water is improved to high quality water by ozone, enters the filtration device (8), the suspended solids are captured in the filter material layer, and the water quality including sterilization, decolorization, and deodorization is improved by ozone and cleaned. It becomes clear water and is returned to the bathhouse.

又一方、ろ過装置(8)のろ材に捕捉された浮遊物質は、
矢印Bの系統により捕捉された物質は、系外へ排出され
る。つまり貯留タンク(19)の逆洗水は、弁(20),循環ポ
ンプ(4),弁(6)よりろ過装置の大部へ入る一方、逆洗水
は弁(22)に分岐されエジェクター(23)に入る、これは前
述の如くオゾン発生器(25)により供給されたオゾンが逆
洗分岐水を一部で更に水質改善を計る一方、オゾン水微
細なオゾン化ガスとなり、弁(20)を経てきた逆洗水と混
合、更に循環ポンプ(4)により混合が促進され、全量が
オゾン水化し、微細気泡は全量に細かく混合した状態と
なる。前記状態の逆洗水はろ過装置(8)の下方より入
り、ろ材を下方より上方へ洗浄するがこのときオゾン水
はろ材層間に捕捉した物質、更にろ材内に発生した微生
物を細菌し、上部へ排出する、しかし洗浄水のみによる
捕捉物質を排出するには、多量の洗浄水が必要である
が、ここで微細な空気、未反応オゾン化ガスの気泡はろ
材層に発生した微生物を細菌すると共に、ろ材を分離し
通気状態を良くする一方、空気の浮上力が加速するた
め、洗浄水のみによる洗浄水水量に比べ大巾に小量の水
量でろ材の洗浄が効率的に除去,清浄回復ができること
になる。
On the other hand, the suspended matter trapped in the filter medium of the filtration device (8)
The substance captured by the system indicated by arrow B is discharged to the outside of the system. That is, the backwash water in the storage tank (19) enters most of the filtering device through the valve (20), the circulation pump (4), and the valve (6), while the backwash water is branched to the valve (22). 23), which is the ozone supplied by the ozone generator (25) as described above, while the backwashing branch water partly improves the water quality, while the ozone water becomes fine ozonized gas, and the valve (20) After mixing with the backwash water that has passed through, the mixing is promoted by the circulation pump (4), the whole amount is turned into ozone water, and the fine bubbles are in a finely mixed state. The backwash water in the above state enters from the lower side of the filtration device (8), and the filter medium is washed from the lower side to the upper side.At this time, the ozone water is a substance trapped between the filter medium layers, and further bacteria generated in the filter medium are bacteria, A large amount of wash water is required to discharge the trapped substances by the wash water only, but the fine air and bubbles of unreacted ozonized gas bacteria the microorganisms generated in the filter medium layer. At the same time, while separating the filter media to improve the ventilation, the levitation force of the air is accelerated, so the cleaning of the filter media is efficiently removed and cleaned and recovered with a much smaller amount of water than the amount of wash water using only wash water. You will be able to

なお、上記実施例では浴場循環水について説明したがこ
れは同様なろ過装置を有し、一過で循環しないものであ
ってもよく、また循環分岐水をろ過装置から出た清浄水
から分岐しオゾンを注入するようにしたが、これは原水
ポンプの吐出側であればよく、更には別系統から、分岐
しオゾン注入できる構造で、オゾン注入後の返送先は、
原水ポンプの吸引側であればよく、又、系統の弁は手動
弁あるいは電動弁であってもよく、更にその配置場所
は、循環水及び洗浄水が分岐通水できる様配置されれば
よい。また上記実施例では浴場に規定の残留塩素を残す
ため、固形塩素投入タンクを設けたがこれは注入するも
のであればよく、又残留塩素の規制がない場合はなくて
も、上記実施例と同様の効果を奏する。
In addition, although the bath circulating water is described in the above embodiment, it may have a similar filtering device and may not circulate in a transient manner, and the circulating branched water is branched from the clean water discharged from the filtering device. Although ozone was injected, this may be on the discharge side of the raw water pump, and it has a structure that allows branching and injection of ozone from another system.
The suction side of the raw water pump may be used, and the valve of the system may be a manual valve or an electric valve, and its location may be such that circulating water and wash water can be branched and passed. Further, in the above-mentioned embodiment, in order to leave the specified residual chlorine in the bath, a solid chlorine input tank was provided, but this may be any one that can be injected, and even if there is no restriction of residual chlorine, it is possible to Has the same effect.

〔発明の効果〕〔The invention's effect〕

以上のように、この発明によれば、水質改善の水処理装
置として原水ポンプ吐出側の循環水の一部にオゾンを注
入し、オゾン化ガスの微細空気量を原水ポンプのキャビ
テーション以内とし、原水ポンプの攪拌混合によりオゾ
ン反応効率を上げることができ、オゾン以外の薬剤の使
用量が皆無かあるいは大巾に低減できるため、浴場内の
塩素濃度も皆無か大巾に低減できる。従って建物に使用
されている金属の腐食、および雰囲気が大巾に改善でき
快的な浴場となる。又、オゾン水及び微細なオゾン化ガ
ス気泡混合の洗浄水によるろ材の洗浄が、少い量で洗浄
回復できるため経済的であり、ろ材内部の微生物細菌を
殺菌するため非常に衛生的な浴場水が得られる効果があ
る。
As described above, according to the present invention, as a water treatment device for improving water quality, ozone is injected into a part of the circulating water on the discharge side of the raw water pump, and the fine air amount of ozonized gas is set within the cavitation of the raw water pump. The ozone reaction efficiency can be increased by stirring and mixing with a pump, and the amount of chemicals other than ozone used can be reduced or greatly reduced, so that the chlorine concentration in the bath can be reduced to a large extent. Therefore, the corrosion of the metal used in the building and the atmosphere can be greatly improved, and the bath becomes a pleasant bath. In addition, it is economical to wash the filter medium with ozone water and washing water containing a mixture of fine ozonized gas bubbles, because it can be recovered by washing in a small amount, and it is very hygienic bath water to sterilize microbial bacteria inside the filter medium. There is an effect that can be obtained.

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

第1図はこの発明による浴場循環水のオゾン水処理装置
を示す配管系統フロー図、第2図は従来の浴場の循環水
水処理装置を示す配管系統フロー図である。 (21)は循環水分岐弁、(22)は逆洗水分岐弁、(23)はエジ
ェクター、(24)は分岐水返送弁、(25)はオゾン発生装
置、(26)はオゾン供給弁、(27)はチャッキ弁。 なお、図中、同一符号は同一、又は相当部分を示す。
FIG. 1 is a piping system flow diagram showing an ozone water treatment device for bath water circulating according to the present invention, and FIG. 2 is a piping system flow diagram showing a conventional circulating water treatment device for a bath. (21) is a circulating water branch valve, (22) is a backwash water branch valve, (23) is an ejector, (24) is a branch water return valve, (25) is an ozone generator, and (26) is an ozone supply valve. (27) is a check valve. In the drawings, the same reference numerals indicate the same or corresponding parts.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】ろ過装置を有し、水の水質改善をするもの
において、原水ポンプの吐出側より原水の一部が分岐で
きる分岐配管を設け、その分岐配管にエジェクターを配
備し、エジェクターの吸引部にオゾン発生器により得ら
れたオゾンを注入混合させ、水をオゾン処理するととも
にオゾン水を造り、オゾン水化した分岐配管を原水ポン
プの吸引側に返送し、原水全量に前述のオゾン水及び未
反応のオゾン化ガスを原水ポンプがキャビテーションを
起こさない範囲で供給しポンプエンペラーの攪拌により
オゾン水による原水全量にオゾン処理及び原水ポンプの
未反応オゾン化ガスの反応促進によりオゾンの吸収効率
を向上させて、オゾンによる水処理ができるように構成
したことを特徴とするオゾン処理装置。
1. A device for improving water quality, comprising a filtering device, wherein a branch pipe for branching a part of the raw water from a discharge side of the raw water pump is provided, and an ejector is provided in the branch pipe to suck the ejector. The ozone obtained by the ozone generator is injected and mixed into the section, water is treated with ozone and ozone water is produced, and the ozone-watered branch pipe is returned to the suction side of the raw water pump, and the above-mentioned ozone water and Unreacted ozonized gas is supplied by the raw water pump within the range where cavitation does not occur, and the stirring of the pump emperor improves the ozone absorption efficiency by treating the entire amount of raw water with ozone water and promoting the reaction of the unreacted ozonized gas in the raw water pump The ozone treatment device is characterized in that the ozone water treatment can be performed.
【請求項2】ろ過装置を有し、そのろ過装置のろ材を定
期的に洗浄するものにおいて、洗浄水の一部が分岐でき
る分岐洗浄配管を設け、その分岐配管にエジェクターを
配備しエジェクターの吸引部にオゾン発生器により得ら
れたオゾンを注入混合させ、オゾン水及び微細なオゾン
化ガス気泡を作り、洗浄水を原水ポンプの吸引側で合流
し原水ポンプにより更に未反応オゾンを吸収混合させ、
ろ材洗浄回路をろ過装置下部に設けた洗浄水供給部より
吐出させることにより、ろ過装置のろ材をオゾン水、お
よびオゾン化ガス微細空気により、ろ材の洗浄およびろ
材に発生した細菌を減菌するように構成したことを特徴
とするオゾン水処理装置。
2. A filter having a filter device for regularly cleaning a filter medium of the filter device, wherein a branch cleaning pipe capable of branching a part of cleaning water is provided, and an ejector is arranged in the branch pipe to suck the ejector. The ozone obtained by the ozone generator is injected and mixed into the section, ozone water and fine ozonized gas bubbles are created, and the wash water is merged on the suction side of the raw water pump, and the unreacted ozone is further absorbed and mixed by the raw water pump,
By discharging the filter medium cleaning circuit from the cleaning water supply unit provided at the bottom of the filter, the filter medium of the filter is cleaned with ozone water and fine air of ozonized gas to clean the filter medium and sterilize bacteria generated in the filter medium. An ozone water treatment device characterized in that
JP62050812A 1987-03-05 1987-03-05 Ozone water treatment equipment Expired - Fee Related JPH0645030B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62050812A JPH0645030B2 (en) 1987-03-05 1987-03-05 Ozone water treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62050812A JPH0645030B2 (en) 1987-03-05 1987-03-05 Ozone water treatment equipment

Publications (2)

Publication Number Publication Date
JPS63166494A JPS63166494A (en) 1988-07-09
JPH0645030B2 true JPH0645030B2 (en) 1994-06-15

Family

ID=12869174

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62050812A Expired - Fee Related JPH0645030B2 (en) 1987-03-05 1987-03-05 Ozone water treatment equipment

Country Status (1)

Country Link
JP (1) JPH0645030B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02290295A (en) * 1989-04-28 1990-11-30 Noritz Corp Apparatus for sterilizing and clarifying bath water
JPH0698353B2 (en) * 1989-04-28 1994-12-07 株式会社ノーリツ Bath water sterilizer
JPH03151094A (en) * 1989-11-06 1991-06-27 Ube Ind Ltd Circulating and cleaning device for bath water
US7984567B2 (en) * 2008-10-07 2011-07-26 Christ Bill Bertakis Apparatus for cleaning simulated hair articles
JP2012527999A (en) * 2009-05-27 2012-11-12 ソン ギュン ムン, Waste water heat recovery device and method

Also Published As

Publication number Publication date
JPS63166494A (en) 1988-07-09

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