JPS6287296A - Complete treatment device for water - Google Patents

Complete treatment device for water

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Publication number
JPS6287296A
JPS6287296A JP60227401A JP22740185A JPS6287296A JP S6287296 A JPS6287296 A JP S6287296A JP 60227401 A JP60227401 A JP 60227401A JP 22740185 A JP22740185 A JP 22740185A JP S6287296 A JPS6287296 A JP S6287296A
Authority
JP
Japan
Prior art keywords
treated water
treatment tank
ozone
treatment
water
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
Application number
JP60227401A
Other languages
Japanese (ja)
Inventor
Keisuke Iwabori
岩堀 恵祐
Yoshiaki Arai
喜明 新井
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.)
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Electric Manufacturing 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 Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Electric Manufacturing Co Ltd
Priority to JP60227401A priority Critical patent/JPS6287296A/en
Publication of JPS6287296A publication Critical patent/JPS6287296A/en
Pending legal-status Critical Current

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  • Physical Water Treatments (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To efficiently execute a complete treatment of secondarily treated water, etc., by constituting a titled device of a filtering treatment tank for treated water, ozone and ultrasonic treatment tank for changing the high mol.wt. material in the treated water to low mol.wt. material and adsorbing treatment tank for the low mol.wt. material in the treated water. CONSTITUTION:A supply port 10 for supplying the treated water is provided to the filtering treatment tank 1 and the first filter media 4 for making the filtering treatment are housed therein. Ozone contactors 11a, 11b which change the high mol.wt. material in the treated water to the low mol.wt. material and an ultrasonic wave generator 28 are housed in the ozone and ultrasonic treatment tank 2 communicated with the tank 1. A discharge port 26 is provided to the adsorbing treatment tank 3 communicated with the tank 2 and the second filter media 20 for adsorbing treatment of the low mol.wt. material in the treated water are housed therein. As a result, the complete treatment of the secondarily treated water, etc., is efficiently executed.

Description

【発明の詳細な説明】 ん産業上の利用分野 本発明は、二次処理水等に更に高次処理を施すための水
の高度処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to an advanced water treatment device for subjecting secondary treated water to higher level treatment.

B0発明の概要 本発明は、二次処理水等に更に高次処理を施すための水
の高度処理装置において、 処理水を濾過処理するための濾過処理槽と、処理水中の
高分子量物質を低分子量物質に変えるオゾン・超音波処
理槽と、処理水中の低分子量物質を吸着処理するための
吸着処理槽とで構成することにより、 二次処理水等の高次処理が効率良く行なわれるようにし
たものである。
B0 Summary of the Invention The present invention provides a filtration treatment tank for filtering treated water, and a method for reducing high molecular weight substances in the treated water, in an advanced water treatment device for subjecting secondary treated water to higher level treatment. By comprising an ozone/ultrasonic treatment tank for converting into molecular weight substances and an adsorption treatment tank for adsorbing low molecular weight substances in the treated water, high-level treatment of secondary treated water etc. can be carried out efficiently. This is what I did.

C0従来の技術 水資源の確保が田畑となってきた今日では、二次処理水
を工業用水として再使用する傾向にある。
C0 Conventional Technology Nowadays, securing water resources has become a chore, and there is a tendency to reuse secondary treated water as industrial water.

しかし、二次処理が効果的に行なわれて水質も良好であ
れば二次処理水をそのまま再利用する上で問題はないが
、以下のような理由により良好な二次処理水が安定して
得られなくなってきた。
However, if the secondary treatment is carried out effectively and the water quality is good, there is no problem in reusing the secondary treated water as it is, but for the following reasons, the quality of the secondary treated water is not stable. I am no longer able to get it.

(イ)二次処理設備への流入量が増大し、流入特性の変
動が大きい。
(b) The amount of inflow to the secondary treatment equipment increases, and the fluctuations in inflow characteristics are large.

(ロ) 生物酸化により処理水が着色される。(b) Treated water is colored due to biological oxidation.

(ハ) NやPに関与した高栄養化の問題が生じている
(c) There is a problem of high nutrition related to N and P.

このような事情にも拘らず、二次処理水を再使用する傾
向は年々高まっている。また、一方では社会的な事情に
よって取水源の水質が悪化しているため、取水源の水を
浄水場へ導いて上水をつくる前に前処理を行なう必要性
が高くなっている。
Despite these circumstances, the trend of reusing secondary treated water is increasing year by year. On the other hand, due to social circumstances, the quality of water at intake sources is deteriorating, making it increasingly necessary to pre-treat the water at intake sources before guiding it to a water treatment plant to produce clean water.

二次処[11j水を高次処理したり上水をつくるために
取水源の水を前処理する、所謂高次処理するためζこ、
従来は次のような方法が用いられている。
Secondary treatment [11j Pre-treatment of water from the intake source in order to perform high-level treatment of water or create tap water, so-called high-level treatment,
Conventionally, the following method has been used.

イ)活性炭吸着法 (ロ)電気透析法 (ハ)逆浸透法 に)凝集沈殿法 (ホ)化学的酸化法 (へ)砂濾過法 り0発明が解決しようとする問題点 ところが、これらの従来の高度処理方法は処理性能が異
なるために単なるこれらの組み合せだけでは目標とする
処理性能を得ることができない。
(b) Activated carbon adsorption method (b) Electrodialysis method (c) Reverse osmosis method) Coagulation precipitation method (e) Chemical oxidation method (f) Sand filtration method Since the advanced processing methods have different processing performance, it is not possible to obtain the target processing performance simply by combining these methods.

そこで本発明は、斯かる問題を解決した水の高度処理装
置を提供することを目的とする。
Therefore, an object of the present invention is to provide an advanced water treatment device that solves such problems.

E0問題点を解決するための手段 斯かる目的を達成するための本発明の構成は、処理水を
供給するための供給口を有するとともに濾過処理を行な
うための第一炉材が収納された濾過処理槽と、該濾過処
理槽へ連通されるとともに処理水中の高分子量物質を低
分子量物質に変えるオゾン接触器と超音波発生器とが収
納されたオゾン・超音波処理槽と、該オゾン・超音波処
理槽に連通されるとともに排出口を有し処理水中の低分
子量物質を吸着処理する第二炉材が収納された吸着処理
槽とから構成されることを特徴とする。
Means for Solving the E0 Problem The structure of the present invention for achieving the above object is a filtration filter having a supply port for supplying treated water and housing a first furnace material for performing filtration treatment. an ozone/ultrasonic treatment tank that communicates with the filtration tank and houses an ozone contactor and an ultrasonic generator that convert high molecular weight substances in the treated water into low molecular weight substances; It is characterized by comprising an adsorption treatment tank that communicates with the sonication treatment tank, has a discharge port, and houses a second furnace material for adsorbing low molecular weight substances in the treated water.

70作 用 二次処理水等の処理水が供給口から濾過処理槽へ流入す
ると、第−炉材によって処理水中に含まれる浮遊物等が
除去される。このあと、処理水はオゾン・超音波処理槽
内でオゾン接触器と超音波発生器によってオゾン処理と
超音波処理され処理水中の高分子量物質が低分子量物質
ζこ変わる。そして、この低分子量物質が吸着処理槽内
の第二戸材によって吸着処理され除去される。
70 Effect When treated water such as secondary treated water flows into the filtration treatment tank from the supply port, suspended matter contained in the treated water is removed by the first furnace material. After this, the treated water is treated with ozone and ultrasonic waves in an ozone/ultrasonic treatment tank using an ozone contactor and an ultrasonic generator, thereby converting the high molecular weight substances in the treated water into low molecular weight substances. Then, this low molecular weight substance is adsorbed and removed by the second door material in the adsorption treatment tank.

以上のようにして高次処理が完了する。The higher-order processing is completed in the above manner.

G、実施例 以下、本発明を図面に示す実施例に基づいて詳細に説明
する。
G. Examples Hereinafter, the present invention will be explained in detail based on examples shown in the drawings.

#ヰ図に示すのは、水の高度処理装置の断面図である。Figure #3 is a cross-sectional view of an advanced water treatment device.

高度処理装置は、濾過処理槽1とオゾン・超音波処理槽
2と吸着処理t1!13とから構成されており、オゾン
・超音波処理槽2は超音波処理槽2aとオゾン処理m2
b、2cとから構成されている。
The advanced treatment equipment is composed of a filtration treatment tank 1, an ozone/ultrasonic treatment tank 2, and an adsorption treatment t1!13, and the ozone/ultrasonic treatment tank 2 includes an ultrasonic treatment tank 2a and an ozone treatment m2.
b, 2c.

濾過処理槽1は、処理水に含まれる浮遊物質(以下、s
sという)や砂(以下、SFとG)う)−を除去する目
的で設けられたものであり、スコ゛ソ千ブライト、スポ
ンジ、カキ殻、タワシ等を袋に詰め込んだ第−炉材4が
、上部に設けた開閉自在の蓋5を134けることによっ
てり換可能に収納されている。第−炉材4として袋に詰
め込むものは、下流へ流入してしまうことを防止するた
め固形タイプでなければならない。−過処理ll!1の
底には沈降したSS分等をためるための排泥ピパノト6
が形成されており、排泥ピット6の下には弁7を介して
逆洗ポンプ8が接続されている。逆洗ポンプ8は、炉材
4がSS分等によって閉塞しな[、)ように洗浄するた
めに設けられている。図中、9はSS分等を排出する丸
めの弁、10は二次処理水を供給するための供給口であ
る。
The filtration treatment tank 1 removes suspended solids (hereinafter referred to as s) contained in the treated water.
It was installed for the purpose of removing sand (hereinafter referred to as SF and G) and sand (hereinafter referred to as SF and G). It is stored in a replaceable manner by closing a lid 5 provided on the top that can be opened and closed. The material packed into the bag as the first furnace material 4 must be of solid type to prevent it from flowing downstream. -Overprocessing! At the bottom of 1, there is a drain pipe 6 for storing sedimented SS, etc.
A backwash pump 8 is connected below the mud removal pit 6 via a valve 7. The backwash pump 8 is provided to clean the furnace material 4 so that it will not be clogged by SS components or the like. In the figure, 9 is a round valve for discharging SS water, etc., and 10 is a supply port for supplying secondary treated water.

オゾン・超音波処理槽2においては、超音波処理槽2a
が下部でヂ過処理槽1と連通し、オゾン処理槽2bが上
部で超音波処理槽2aと連通し、オゾン処理槽2bと2
Cとが上下で連通している。
In the ozone/ultrasonic treatment tank 2, the ultrasonic treatment tank 2a
communicates with the overtreatment tank 1 at the bottom, the ozone treatment tank 2b communicates with the ultrasonic treatment tank 2a at the top, and the ozone treatment tanks 2b and 2
C is connected at the top and bottom.

超音波処理12aの底部には超音波発生器28が設置さ
れ、オゾン処理槽2b、2Cの底には夫々オゾン接触器
11a、llbが設置されている。
An ultrasonic generator 28 is installed at the bottom of the ultrasonic treatment 12a, and ozone contactors 11a and llb are installed at the bottoms of the ozone treatment tanks 2b and 2C, respectively.

オゾン接触aL1a、11bは、処理水とオゾンとが接
触する機会をできるだけ多くするために具えられており
、底面に置かれた散気板12が供給管13を介してオゾ
ン・超音波処理槽2の外部に具えられたオゾン発生器1
4と接続されている。超音波処理槽2 atオゾン処理
槽2b、2Cの上部は密閉されており、この上部には弁
15を介して排気ポンプ[6が接続され、更に該排気ポ
ンプ16と排オゾン処理器17とオゾン発生器14とが
三方弁18を介して接続さねている。
The ozone contacts aL1a and 11b are provided to increase the chances of contact between the treated water and ozone. Ozone generator 1 provided externally
4 is connected. The upper part of the ultrasonic treatment tank 2 at the ozone treatment tank 2b, 2C is sealed, and an exhaust pump [6 is connected to this upper part via a valve 15, and the exhaust pump 16, the exhaust ozone processor 17, and the ozone A generator 14 is connected via a three-way valve 18.

なお、本実施例ではオゾン・超音波処理槽2を三種式と
してオゾン接触器を二組具えた場合について示したが、
処理水の量が少ない場合は一槽式吸着処理槽3は、次の
目的で設けられたものである。即ち、二次処理によって
生成した高分子量物質がオゾン・超音波処理槽2で低分
子化されるので、この低分子化された物質を除去するこ
とにある。
In addition, in this example, the case is shown in which the ozone/ultrasonic treatment tank 2 is of three types and is equipped with two sets of ozone contactors.
When the amount of treated water is small, the single-tank adsorption treatment tank 3 is provided for the following purpose. That is, since the high molecular weight substances generated by the secondary treatment are reduced in molecular weight in the ozone/ultrasonic treatment bath 2, the aim is to remove this reduced molecular weight substance.

吸着処理槽3の上部lこは処理水を散布するための散布
トイ19が設けられ、散布トイ19の下には第二炉材2
0が配置されている。第二炉材20は低分子量物質を吸
着するものであり、活性炭を用いるのが望ましいが、活
性炭は高価なので鹿沼土、火山岩等の吸着能力を有する
ものを混合又は階層化して用いると経済的である。第二
炉材20の真下には消毒タンク21から伸びるパイプ2
2の先端が臨んでおり、吸着槽3の底には排泥ピット%
が形成され、弁24が取り付けられている。なお、25
は第二炉材20を交換するための蓋、26は高度処理さ
れた処理水を排出する排出口である。
A sprinkling toy 19 for sprinkling treated water is provided in the upper part of the adsorption treatment tank 3, and below the sprinkling toy 19 is a second furnace material 2.
0 is placed. The second reactor material 20 is one that adsorbs low molecular weight substances, and it is desirable to use activated carbon, but since activated carbon is expensive, it is economical to mix or layer materials with adsorption capacity, such as Kanuma soil or volcanic rock. be. Directly below the second furnace material 20 is a pipe 2 extending from the disinfection tank 21.
The tip of 2 is facing, and the bottom of adsorption tank 3 is a sludge pit.
is formed and a valve 24 is attached. In addition, 25
2 is a lid for replacing the second furnace material 20, and 26 is an outlet for discharging the highly treated treated water.

前記のようにオゾン・超音波処理槽2はオゾンが大気中
へ放出されないように密閉構造とする必要があり、その
ためにオゾン処理槽2Cと吸着処理槽3とを連通させる
目的で、水面よ6つ低G)位置に越流部27を設けてい
る。
As mentioned above, the ozone/ultrasonic treatment tank 2 needs to have a sealed structure to prevent ozone from being released into the atmosphere, and for this reason, in order to communicate the ozone treatment tank 2C and the adsorption treatment tank 3, it is necessary to An overflow portion 27 is provided at the lower G) position.

次に、斯かる水の高度処理装置の作用を説明する。Next, the operation of such an advanced water treatment device will be explained.

供給口10から濾過処理槽1内へ二次処理された処理水
が流入し、瀉−炉材4の内部を流れることζこより浮遊
しているSS分や87分が濾過されて除去される。
Secondary treated treated water flows into the filtration treatment tank 1 from the supply port 10 and flows inside the sieve material 4, whereby floating SS and 87 water are filtered and removed.

SS分等が除去された処理水は濾過処理槽1の下部から
オゾン・超音波処理槽2内へ流入しオゾン処理及び超音
波処理される。超音波処理槽2aでは、処理水は上向流
として流れながら超音波発生器28によって超音波処理
される。超音波発生器28は連続して動作させる必要は
なく、処理水が連続的に流入する場合は超音波処理槽2
aの容積と流入量との割合(超音波処理槽2aにおける
水理学的滞留時間)で間欠運転し、処理水が間欠的に流
入する場合は流入時のみ運転すればよい。オゾン処理m
2に+、2Qでは、オゾン発生器14から供給管13を
介して散気板12へ送られたオゾンが散気板12から処
理水中を上昇し、処理水と効率良く接触する。処理水と
接触したオゾンは、オゾン・超音波処理槽2の上部にた
まり、排気ポンプ16によって排オゾン処理器17に送
られ処理後大気中へ放出されるか、又はオゾン発生器1
4へと送られる。
The treated water from which SS components and the like have been removed flows into the ozone/ultrasonic treatment tank 2 from the lower part of the filtration treatment tank 1 and is subjected to ozone treatment and ultrasonic treatment. In the ultrasonic treatment tank 2a, the treated water is subjected to ultrasonic treatment by the ultrasonic generator 28 while flowing upward. The ultrasonic generator 28 does not need to be operated continuously, and if the treated water continuously flows into the ultrasonic treatment tank 2.
It is operated intermittently at the ratio of the volume of a to the inflow amount (hydraulic residence time in the ultrasonic treatment tank 2a), and when treated water intermittently flows in, it is sufficient to operate only when the water flows in. Ozone treatment
At 2+ and 2Q, ozone sent from the ozone generator 14 to the air diffuser plate 12 via the supply pipe 13 rises from the air diffuser plate 12 into the treated water and efficiently contacts the treated water. Ozone that has come into contact with the treated water accumulates in the upper part of the ozone/ultrasonic treatment tank 2, is sent to the exhaust ozone treatment device 17 by the exhaust pump 16, and is discharged into the atmosphere after treatment, or is removed from the ozone generator 1.
Sent to 4.

使用済みのオゾンを処理して大気中へ放出するかそれと
もオゾン発生器14へ戻して再使用するかは、三方*i
sの操作によって決まる。つまり、三方弁18は排気ポ
ンプt6と排オゾン処理器17又は排気ポンプ16とオ
ゾン発生器14とを接続するものである。
Whether the used ozone is processed and released into the atmosphere or returned to the ozone generator 14 for reuse is determined by the three parties *i.
Determined by the operation of s. That is, the three-way valve 18 connects the exhaust pump t6 and the exhaust ozone processor 17 or the exhaust pump 16 and the ozone generator 14.

使用済みのオゾンが再使用できるので、オゾンの無駄が
なく、排オゾン処理器17の負担も少ない。
Since used ozone can be reused, no ozone is wasted and the burden on the exhaust ozone processor 17 is reduced.

二組のオゾン接触器11a、111)によって、処理水
はオゾン処理及び超音波処理され、処理水に含まれてい
る高分子量物質(Too成分)が低分子量物質となり、
越流部27から吸着処理槽3へと流入する。
The treated water is subjected to ozone treatment and ultrasonic treatment by two sets of ozone contactors 11a and 111), and the high molecular weight substances (Too component) contained in the treated water become low molecular weight substances,
It flows into the adsorption treatment tank 3 from the overflow section 27 .

吸着処理槽3では、処理水が散布トイ19から第二濾材
20へ向かって散布され、オゾン・超音波処理槽2内に
おいて、低分子化された処理水中の低分子量物質が第二
炉材20に吸着され除去される。
In the adsorption treatment tank 3 , the treated water is sprayed from the spray toy 19 toward the second filter material 20 , and in the ozone/ultrasonic treatment tank 2 , the low molecular weight substances in the treated water are reduced to a second furnace material 20 . is absorbed and removed.

吸着処理槽3では分子flk5000  以上(Fl)
のTOC成分と分子m5oo以下(F3)の無機成分は
除去できないが、分子t 500〜5000(F2)と
分子量500以下(F3)のTOC成分の除去には有効
である。以上のようにして高度処理された処理水は、必
要に応じて消毒タンク21内の消粘液で消毒され、排出
口26より排出される。
In adsorption treatment tank 3, molecular flk5000 or more (Fl)
Although it cannot remove TOC components with a molecular weight of 500 to 5000 (F2) and inorganic components with a molecular weight of 500 or less (F3), it is effective in removing TOC components with a molecular weight of 500 to 5000 (F3). The treated water that has been highly treated as described above is disinfected with the deviscosity solution in the disinfection tank 21 as required, and is discharged from the discharge port 26.

排泥ピット6や23に沈降したSS分等がたまつた場合
は、これらを弁9や24を開いて排出すればよい。また
、長期間のコ4転によって第−七炉材4が目づまりをお
こした場合は、弁7を開いて3fI!洗ポンプ8を用い
て第一7P材4を洗浄し、第一濾材4用した後は蓋5.
25を開いて交換すればよい。
If sedimented SS and the like accumulate in the mud removal pits 6 and 23, they can be discharged by opening the valves 9 and 24. In addition, if the No. 7 furnace material 4 becomes clogged due to long-term rotation, open the valve 7 and press 3fI! After washing the first 7P material 4 using the washing pump 8 and using the first filter material 4, the lid 5.
25 and replace it.

なお、本実施例では二次処理水を高度処理する水 場合について示したが、上節を得るための取水源の水を
高度処理する場合にも適用できる。
In this embodiment, the case where the secondary treated water is subjected to advanced treatment is shown, but the present invention can also be applied to the case where the water from the intake source for obtaining the above-mentioned water is subjected to advanced treatment.

H1発明の詳細 な説明したように本発明によれば、処理水が濾過処i榴
、オゾン・超音波処理槽、吸着処理槽の順に流れるので
、8B、Sr分が除去されて処理水中の高分子量物質が
低分子化されたのちに低分子量物質が吸着されて除去さ
れることになって水が確実ζこ高度処理される。
According to the present invention, as described in detail of the H1 invention, the treated water flows in the order of the filtration treatment tank, the ozone/ultrasonic treatment tank, and the adsorption treatment tank, so that the 8B and Sr components are removed and the high concentration in the treated water is reduced. After the molecular weight substances are reduced to low molecular weight substances, the low molecular weight substances are adsorbed and removed, thereby ensuring that the water is treated at a high level.

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

図は本発明による水の高度処理装置の実施例を示す断面
図である。 1・・・濾過処理槽、2・・・オゾン・超音波処理槽、
2a・・・超音波処理槽、2b、2C・・・オゾン処理
槽、3・・吸着処理槽、4・・・第−弁材、10・・・
供給口、111!L11 ?)・・・オゾン接触器、1
3・・・供給管、14・・・オゾン発生器、20・・第
二戸材、28・・超音波発生器。
The figure is a sectional view showing an embodiment of the advanced water treatment apparatus according to the present invention. 1...filtration treatment tank, 2...ozone/ultrasonic treatment tank,
2a... Ultrasonic treatment tank, 2b, 2C... Ozone treatment tank, 3... Adsorption treatment tank, 4... No. 1 valve material, 10...
Supply port, 111! L11? )...Ozone contactor, 1
3... Supply pipe, 14... Ozone generator, 20... Second door material, 28... Ultrasonic generator.

Claims (1)

【特許請求の範囲】[Claims] 処理水を供給するための供給口を有するとともに濾過処
理を行なうための第一濾材が収納された濾過処理槽と、
該濾過処理槽へ連通されるとともに処理水中の高分子量
物質を低分子量物質に変えるオゾン接触器と超音波発生
器とが収納されたオゾン・超音波処理槽と、該オゾン・
超音波処理槽に連通されるとともに排出口を有し処理水
中の低分子量物質を吸着処理する第二濾材が収納された
吸着処理槽とから構成されることを特徴とする水の高度
処理装置。
a filtration treatment tank having a supply port for supplying treated water and housing a first filter medium for performing filtration treatment;
an ozone/ultrasonic treatment tank that communicates with the filtration treatment tank and houses an ozone contactor and an ultrasonic generator for converting high molecular weight substances in the treated water into low molecular weight substances;
1. An advanced water treatment device comprising an adsorption treatment tank that communicates with an ultrasonic treatment tank, has a discharge port, and houses a second filter medium for adsorbing low molecular weight substances in treated water.
JP60227401A 1985-10-11 1985-10-11 Complete treatment device for water Pending JPS6287296A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60227401A JPS6287296A (en) 1985-10-11 1985-10-11 Complete treatment device for water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60227401A JPS6287296A (en) 1985-10-11 1985-10-11 Complete treatment device for water

Publications (1)

Publication Number Publication Date
JPS6287296A true JPS6287296A (en) 1987-04-21

Family

ID=16860249

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60227401A Pending JPS6287296A (en) 1985-10-11 1985-10-11 Complete treatment device for water

Country Status (1)

Country Link
JP (1) JPS6287296A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100301299B1 (en) * 1999-06-30 2001-09-22 김창규 Device for treating a swage and waste water of unhigh density and trouble resovability
KR100788849B1 (en) * 2006-08-22 2007-12-27 오엑스엔지니어링(주) Water treatment apparatus by ozone
JP2011072982A (en) * 2008-12-02 2011-04-14 Shozo Katakura Sewage treatment system and fine air bubble generator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100301299B1 (en) * 1999-06-30 2001-09-22 김창규 Device for treating a swage and waste water of unhigh density and trouble resovability
KR100788849B1 (en) * 2006-08-22 2007-12-27 오엑스엔지니어링(주) Water treatment apparatus by ozone
JP2011072982A (en) * 2008-12-02 2011-04-14 Shozo Katakura Sewage treatment system and fine air bubble generator

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