JPH07185573A - System and method for treating water - Google Patents

System and method for treating water

Info

Publication number
JPH07185573A
JPH07185573A JP33838893A JP33838893A JPH07185573A JP H07185573 A JPH07185573 A JP H07185573A JP 33838893 A JP33838893 A JP 33838893A JP 33838893 A JP33838893 A JP 33838893A JP H07185573 A JPH07185573 A JP H07185573A
Authority
JP
Japan
Prior art keywords
water
ozone
treated
treatment
treatment device
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
JP33838893A
Other languages
Japanese (ja)
Inventor
Masayoshi Kubota
昌良 久保田
Tetsuro Haga
鉄郎 芳賀
Masahiko Ishida
昌彦 石田
Kenji Baba
研二 馬場
Minoru Suzuki
実 鈴木
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP33838893A priority Critical patent/JPH07185573A/en
Publication of JPH07185573A publication Critical patent/JPH07185573A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To improve a sterilization effect for a bacteria that exists in water to be treated in a water treating system. CONSTITUTION:The water is taken from a lake or river 100 in a channel pond 111, and added with a floculant 110 to make micro suspended matters in the water into floc in a floc forming pond 112, and it is induced to a coagulator pond 113, and subjected to sedimentation, then, it is filtered in a sand filter pond 114. Treatment up to such step is a conventional clean water treating process. In addition to that a magnetization processor 1 is arranged at the preceding stage of an ozone processor 2. The water filtered by the sand filter pond 114 is subjected to magnetization treatment by the magnetization device 1, and then is subjected to ozone treatment by blowing ozonized air from an ozone generator 3 in an ozone reaction tank 2. The water treated with ozone treatment is purified by a bio-activated carbon tower 5, and it is sterilized by a chlorine 115 in a treating water tank 116, then, it is supplied as city water via a water supply pump 117.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、飲料用上水道またはプ
ール水の浄化、並びに下水道の再利用水等の浄化に用い
られる水処理システム、および水処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment system and a water treatment method used for the purification of drinking water or pool water, and the purification of recycled water of sewers.

【0002】[0002]

【従来の技術】近年、湖沼や河川の汚濁が進行し、富栄
養化によってプランクトンが繁殖することにより、カビ
臭等の異臭味の発生や溶存有機物濃度が高くなり、安全
でおいしい水を供給するためオゾン・生物活性炭による
高度浄水処理システムの導入が、特に大都市圏で計画あ
るいはすでに開始されつつある。ここで、オゾン処理に
よって形成される反応生成物に関する情報が少なく、そ
れらの安全性に対する危惧から、オゾン利用については
活性炭処理の併設が国によって指導されている。また、
オゾンを利用した処理法には下水処理場の二次処理水を
中水として多目的に再利用するための下水高度処理、あ
るいはし尿処理水や染色排水の殺菌及び脱色に検討され
ている。その他、熱交換器や冷却水系などの管路に発生
する生物付着防止にオゾン法が注目されている。
2. Description of the Related Art In recent years, pollution of lakes and rivers has progressed, and plankton has propagated due to eutrophication, resulting in generation of off-flavors such as musty odor and concentration of dissolved organic matter, and supply of safe and delicious water. Therefore, the introduction of advanced water purification systems using ozone and biological activated carbon is being planned or already started, especially in metropolitan areas. Here, there is little information on the reaction products formed by ozone treatment, and because of concern about their safety, the government has instructed the use of ozone for the use of activated carbon treatment. Also,
The treatment method using ozone is being studied for advanced sewage treatment for multipurpose reuse of secondary treated water from sewage treatment plants, or sterilization and decolorization of treated human waste water and dyed wastewater. In addition, the ozone method has been attracting attention for preventing biofouling that occurs in pipes such as heat exchangers and cooling water systems.

【0003】オゾンは、フッ素に次ぐ強い酸化力によ
り、一般に水中の有機物の酸化分解除去や脱色、脱臭、
殺菌を目的に使用されている。例えば、上水でのオゾン
処理の主な目的としては、異臭味除去、フミン質な
どによる着色成分の分解・脱色、有機塩素化合物生成
量の低減、溶解性の鉄、マンガン化合物を酸化し、不
溶性の化合物にする、有機物の生物分解性の向上、な
どがあげられる。
Ozone has a strong oxidizing power second to fluorine, and generally, oxidative decomposition and removal of organic matter in water, decolorization, deodorization,
Used for sterilization purposes. For example, the main purposes of ozone treatment with tap water are removal of off-flavors, decomposition and decolorization of coloring components due to humic substances, reduction of organic chlorine compound production, oxidation of soluble iron and manganese compounds, and insolubility. To improve the biodegradability of organic substances.

【0004】上記はオゾン単独で十分処理効果を発
揮するが、は後段での処理すなわち生物活性炭に
よる処理が必要である。特に、オゾンが有機物と反応す
ると、多くの場合カルボン酸、ケトン、アルデヒドが生
成される。これらのうち、アルデヒド類についてはその
有害性が指摘されおり、上水道の高度浄水処理では活性
炭処理の併設が必須となっている。
[0004] Although ozone alone exerts a sufficient treatment effect, it requires a treatment in a later stage, that is, treatment with biological activated carbon. In particular, when ozone reacts with organic substances, carboxylic acids, ketones, and aldehydes are often produced. Of these, aldehydes have been pointed out to be harmful, and it is essential to install activated carbon treatment in advanced water treatment of water supply.

【0005】一方、水に磁界を作用させると水は特異な
物性を示すとされ、多くの学者の研究対象となり、一時
期話題を集めた。物理化学的に確証が得られていない現
象であるが、多くの応用例が報告され、実用化あるいは
多数の特許が出願されており、各種の磁化処理器が市販
されている。代表的な適用例として、1)磁気処理水の
プールへの適用例(特開昭52-71854号公報,57-29227号
公報)、2)バイオ、養殖等の生体系への適用例(特開
昭64-56189号公報,特開平2-39887号公報,特開平1-299
688号公報,特開平1-34629号公報,特開平1-262988号公
報)、3)磁化コンクリートへの適用例、4)磁化水に
よるスケール防止への適用例(特開平1-184291号公
報)、5)磁化水の赤錆防止への適用例、6)燃料油磁
化への適用例、等々である。特に、磁化処理水がスケー
ル防止に効果があるとされており、スケール防止用磁気
処理装置への適用例の報告が多い。
On the other hand, when a magnetic field is applied to water, it is said that water exhibits unique physical properties, and it has been the subject of many scholars' research and has been a topic for a while. Although this is a phenomenon for which physicochemical confirmation has not been obtained, many application examples have been reported, practical applications or numerous patents have been filed, and various magnetization processors are commercially available. As typical application examples, 1) application examples to magnetically treated water pools (JP-A-52-71854 and 57-29227), 2) application examples to biological systems such as biotechnology and aquaculture (special features JP-A-64-56189, JP-A-2-39887, JP-A1-299
688, JP-A-1-34629, JP-A 1-262988), 3) Application example for magnetized concrete, 4) Application example for scale prevention by magnetized water (JP-A-1-184291) 5) Examples of application of magnetized water to prevention of red rust, 6) Examples of application to fuel oil magnetization, and so on. In particular, magnetized water is said to be effective in preventing scale, and there are many reports of application examples to magnetic processing devices for scale prevention.

【0006】磁化処理及びオゾン処理の両者を利用した
ものとしては、特開平1-262987号公報に示された冷却水
浄化装置がある。これは、冷却塔の循環冷却水の一部を
分岐してろ過・オゾン処理し、他の循環水は磁気処理し
た後、前記オゾン処理水を磁気処理した処理水と合流さ
せるもので、オゾン処理及び磁化処理のそれぞれを並列
に行うようにしたシステムである。その他、オゾンと紫
外線、電子線、触媒併用による処理方法などの研究発表
例がある(たとえば、化学工学,Vol.55,No.9,1991)。
A cooling water purifying apparatus disclosed in Japanese Patent Application Laid-Open No. 1-262987 is one that utilizes both the magnetization treatment and the ozone treatment. This is to circulate a part of the circulating cooling water of the cooling tower for filtration and ozone treatment, and to magnetically treat the other circulating water, and then to join the ozone-treated water with the magnetically treated water. And the magnetization processing is performed in parallel. In addition, there are examples of research presentations on treatment methods using ozone and ultraviolet rays, electron beams, and catalysts (for example, Chemical Engineering, Vol.55, No.9, 1991).

【0007】[0007]

【発明が解決しようとする課題】しかしながら、上記従
来技術では、オゾン処理と磁化処理のそれぞれを並列に
行っているので、殺菌効果が十分ではない。すなわち、
処理水に磁界を与えると水中の生細菌の挙動が不活性化
し、生細菌の増殖を抑制するとの報告があるが、その磁
界を与える磁化処理をオゾン処理から切り離して単独で
行っても、十分な殺菌効果は期待できない。また、磁化
処理についての効果を確証する理論的背景がなく、十分
な効果を保証することが難しいといった問題がある。
However, in the above-mentioned conventional technique, the ozone treatment and the magnetization treatment are performed in parallel, so that the sterilizing effect is not sufficient. That is,
It has been reported that when a magnetic field is applied to the treated water, the behavior of live bacteria in the water is inactivated and the growth of live bacteria is suppressed. You can not expect a good bactericidal effect. Further, there is no theoretical background for confirming the effect of the magnetization process, and it is difficult to guarantee a sufficient effect.

【0008】本発明の目的は、処理対象水の中に存在す
る細菌に対して、その殺菌効果を十分に向上させること
ができる水処理システムおよび水処理方法を提供するこ
とである。
[0008] An object of the present invention is to provide a water treatment system and a water treatment method capable of sufficiently improving the bactericidal effect on bacteria existing in water to be treated.

【0009】[0009]

【課題を解決するための手段】上記目的の達成のため、
本発明は、処理対象水をオゾンで殺菌処理するオゾン処
理装置を備えた水処理システムにおいて、前記処理対象
水の中に存在する細菌類に対して磁気エネルギを与える
磁化処理装置を、処理対象水の流れに沿って前記オゾン
処理装置の前段又は後段の一方に、もしくは前段および
後段の両方に配置したものである。
[Means for Solving the Problems] To achieve the above object,
The present invention relates to a water treatment system provided with an ozone treatment device for sterilizing water to be treated with ozone, wherein a magnetizing treatment device for giving magnetic energy to bacteria present in the water to be treated is treated water. Along the flow of 1., the ozone treatment apparatus is arranged at one of the front stage and the rear stage, or both at the front stage and the rear stage.

【0010】また、本発明は、上記構成の水処理システ
ムにおいて、処理対象水の中に存在する細菌類に対して
磁気エネルギを与える磁化処理装置を、処理対象水の流
れに沿ってオゾン処理装置の前段に配置するとともに、
前記磁化処理装置で磁化処理した処理対象水の一部を前
記オゾン処理装置に導くようにしたものである。
In the water treatment system having the above structure, the present invention provides a magnetizing treatment device for applying magnetic energy to bacteria existing in the water to be treated, which is an ozone treatment device along the flow of the water to be treated. While arranging it in the front stage of
A part of the water to be treated which has been magnetized by the magnetizing device is guided to the ozone treating device.

【0011】また、本発明は、上記構成の水処理システ
ムにおいて、処理対象水の中に存在する細菌類に対して
磁気エネルギを与える磁化処理装置を、処理対象水の流
れに沿ってオゾン処理装置の後段に配置するとともに、
前記オゾン処理装置で殺菌処理した処理対象水の一部を
前記磁化処理装置に導くようにしたものである。
In the water treatment system having the above structure, the present invention further comprises a magnetizing treatment device for applying magnetic energy to bacteria existing in the water to be treated, which is an ozone treatment device along the flow of the water to be treated. It is placed in the latter part of the
A part of the water to be treated that has been sterilized by the ozone treatment device is guided to the magnetization treatment device.

【0012】また、本発明は、上記構成の水処理システ
ムにおいて、処理対象水の中に存在する細菌類に対して
磁気エネルギを与える磁化処理装置を設けるとともに、
オゾン処理装置で殺菌処理した処理対象水の一部を磁化
処理装置に導き、前記磁化処理装置で磁化処理した処理
対象水を前記オゾン処理装置の前段側へ戻すようにした
ものである。
Further, the present invention provides the water treatment system having the above-mentioned structure, further comprising a magnetizing treatment device for giving magnetic energy to bacteria existing in the water to be treated,
A part of the water to be treated that has been sterilized by the ozone treatment device is guided to the magnetization treatment device, and the treatment target water that has been magnetized by the magnetization treatment device is returned to the previous stage side of the ozone treatment device.

【0013】さらに、本発明は、上記水処理システムの
いずれかを、下水の一部を中水とする下水二次処理水高
度処理システム、またはプール水を浄化するプール用水
浄化システムに用いたものである。
Further, according to the present invention, any one of the above-mentioned water treatment systems is used in a sewage secondary treated water advanced treatment system in which a part of sewage is treated as sewage or in a pool water purification system for purifying pool water. Is.

【0014】さらにまた、本発明は、処理対象水をオゾ
ンで殺菌処理する水処理方法において、前記処理対象水
の中に存在する細菌類に対して磁気エネルギを与える磁
化処理を、前記殺菌処理を行う前又は後のどちらか一方
で、もしくは前後の両方で行うことである。
Furthermore, the present invention is a water treatment method for sterilizing water to be treated with ozone, wherein the sterilizing treatment is a magnetizing treatment for imparting magnetic energy to bacteria present in the water to be treated. Before or after, or both before and after.

【0015】[0015]

【作用】本発明は、オゾンによる酸化力と磁気エネルギ
ーによる相乗効果に着目したものである。磁化処理につ
いての効果を確証するものはないが、ファラデーの理論
をもとにした電磁流体力学(MHD発電)から、磁界中
をある流速で水が通過すると、水中の生細菌などに対す
る磁気エネルギーショックが生じることは想像される。
これに加えて、強力なオゾンで酸化すれば殺菌効果は大
である。
The present invention focuses on the synergistic effect of the oxidizing power of ozone and magnetic energy. Although there is no one that confirms the effect of magnetizing treatment, from magnetohydrodynamics (MHD power generation) based on Faraday's theory, when water passes through a magnetic field at a certain flow velocity, magnetic energy shock to live bacteria in the water Is expected to occur.
In addition to this, if it is oxidized with strong ozone, the bactericidal effect is great.

【0016】下水二次処理水により実験検討した結果、
磁化−オゾンと直列で処理することにより、オゾンの殺
菌効果が増大することが確認できた。さらに、他の効果
として磁化による凝集性についても同様に実験を行い、
水中の懸濁物(カオリン添加)のζ電位が変化するとい
う新たな知見が得られた。すなわち、水中の溶解性の鉄
イオンや塩類が、オゾンにより酸化されて不溶性の化合
物となり、これらが磁界を通過すると凝集され沈殿物と
なることから、後処理での除去が容易になると予想でき
る。
As a result of an experimental study with the secondary treated sewage water,
It was confirmed that the bactericidal effect of ozone was increased by the treatment with magnetization and ozone in series. Furthermore, as another effect, the same experiment was performed for the cohesiveness due to magnetization,
A new finding was obtained that the ζ potential of a suspension in water (addition of kaolin) changes. That is, since soluble iron ions and salts in water are oxidized by ozone to become insoluble compounds, which are aggregated and become a precipitate when passing through a magnetic field, it can be expected that removal by post-treatment will be easy.

【0017】本発明は、上記の実験結果からなされたも
ので、磁化とオゾン処理を直列に行うことでオゾンによ
る殺菌処理効果の大幅な向上、及びその他の効果が期待
できる。
The present invention has been made based on the above experimental results, and by performing magnetization and ozone treatment in series, it is possible to expect a great improvement in the sterilization effect by ozone and other effects.

【0018】また、オゾン処理装置で殺菌処理した処理
対象水の一部を磁化処理装置に導く構成、または磁化処
理装置で磁化処理した処理対象水の一部をオゾン処理装
置に導く構成とすれば、磁化処理装置による処理量また
はオゾン処理による処理量を軽減できる。オゾン処理装
置で殺菌処理した処理対象水の一部を磁化処理装置で磁
化処理してからオゾン処理装置の前段側へ戻す場合も、
同様に磁化処理装置による処理量を軽減できる。
If a part of the water to be treated that has been sterilized by the ozone treatment device is guided to the magnetization treatment device, or a part of the water to be treated that has been magnetized by the magnetization treatment device is introduced to the ozone treatment device. The processing amount by the magnetization processing device or the processing amount by the ozone treatment can be reduced. When returning part of the water to be treated that has been sterilized by the ozone treatment device to the previous stage of the ozone treatment device after magnetization treatment with the magnetization treatment device,
Similarly, the amount of processing by the magnetization processing device can be reduced.

【0019】[0019]

【実施例】本発明の効果を実証すべく、以下の実験を行
った。磁化及びオゾン処理の組合せにより、特に生細菌
の分解除去性能に着目し、下水二次処理水を供試して実
験を行った。実験方法を図11に示す。反応セパラブル
フラスコ2(容量5リットル)に、オゾンの懸濁物(S
S)に対する影響を少なくするため砂ろ過をかけた下水
二次処理水4リットルを供試した。オゾン発生器3は
0.8g/Nm3−オゾン化空気1リットル/min(0.8
mgO3/リットル空気)を流量計23を介してフラスコ
2底部のセラミック製散気管から吹き込み、フラスコ2
上部から排オゾンガスとして排気した。気相の発生−排
オゾン濃度測定は配管を切換えることにより行い、さら
に排オゾン濃度及び溶存オゾン濃度とも隔膜形ポーラロ
グラフ電極式の気相用3a、溶存用3bの各オゾン濃度
計により測定した。
EXAMPLES The following experiments were conducted in order to demonstrate the effects of the present invention. By combining magnetization and ozone treatment, paying particular attention to the decomposition and removal performance of live bacteria, an experiment was conducted using secondary treated sewage water. The experimental method is shown in FIG. In a reaction separable flask 2 (5 liters in volume), a suspension of ozone (S
In order to reduce the influence on S), 4 liters of sewage secondary treated water subjected to sand filtration was tested. Ozone generator 3 is 0.8 g / Nm 3 -Ozonized air 1 liter / min (0.8
(mgO 3 / liter air) was blown into the flask 2 from the ceramic air diffuser at the bottom of the flask 2 via the flow meter 23.
It was exhausted as exhaust ozone gas from the upper part. Gas phase generation-Exhaust ozone concentration measurement was performed by switching the pipes, and both the exhaust ozone concentration and the dissolved ozone concentration were measured by a diaphragm-type polarographic electrode-type ozone concentration meter for gas phase 3a and dissolved ozone concentration 3b.

【0020】下水二次処理水はポンプにより200ミリ
リットル/minで循環し、ポンプ7の吐出側に市販の磁
化処理器1を配置し、回分処理式とした。実験は、磁化
処理させつつポンプ7で下水二次処理水を循環させ、オ
ゾン化空気を3方切換え弁8でオゾン濃度計に流通さ
せ、発生オゾン濃度が一定になった時点で切換え、散気
管から吹込んだ。適宜の時間毎にサンプリングして、特
に大腸菌の残存数で殺菌効果について評価した。大腸菌
の培養には、デシオキシコーレート寒天培地を用いた。
なお、図中、20,21はセル、22は切換え弁であ
る。
The sewage secondary treated water was circulated at a rate of 200 ml / min by a pump, and a commercially available magnetization treatment device 1 was arranged on the discharge side of the pump 7 to make it a batch treatment type. In the experiment, the sewage secondary treated water was circulated by the pump 7 while magnetizing, and the ozonized air was circulated to the ozone concentration meter by the three-way switching valve 8 and switched when the generated ozone concentration became constant. I blew from. Sampling was carried out at appropriate times, and the bactericidal effect was evaluated by the number of remaining E. coli. A decioxycholate agar medium was used for culturing Escherichia coli.
In the figure, 20 and 21 are cells, and 22 is a switching valve.

【0021】図12に実験結果を示す。有機物共存下
(COD濃度10ppm)でのオゾン単独と磁化・オゾン
処理による実験結果を大腸菌群数とオゾン濃度・時間積
(CT値)の関係で示した。下水二次処理水には、大腸
菌が103個/ミリリットル程度存在している。CT値
の増加にともない大腸菌群は指数関数的に減少するが、
磁化・オゾン処理による方が傾きが急である。さらに、
顕著な効果として、オゾン単独処理の処理水をフラスコ
内に一昼夜放置すると大腸菌が再増殖するが、磁化とオ
ゾンの流通処理水は一昼夜放置しても変化はなく、むし
ろ検出不可となる。このことは、磁化処理通過の際の磁
気的エネルギーショックにより細菌類の生存エネルギー
が減少し、加えて強力なオゾン酸化により分解されるた
め、両者の相乗効果により効率よく殺菌され、その効果
が持続するものと考えられる。
The experimental results are shown in FIG. Experimental results of ozone alone and magnetization / ozone treatment in the coexistence of organic matter (COD concentration 10 ppm) are shown.
(CT value). The sewage secondary treated water contains approximately 10 3 E. coli / ml. Although the coliform group decreases exponentially with the increase of CT value,
The slope is steeper when magnetized and ozone treated. further,
As a remarkable effect, when the treated water treated with ozone alone is left in the flask for one day and night, the E. coli re-proliferates, but the treated water for magnetization and ozone does not change even if left for one day and becomes undetectable. This is because the survival energy of bacteria is reduced by the magnetic energy shock when passing through the magnetization process and is decomposed by strong ozone oxidation. It is supposed to do.

【0022】この場合、オゾン処理と磁化処理の両者一
対で処理することが重要である。このことは、従来例
(例えば、特開平1-262987号公報)によるオゾン処理と
磁化処理の並列処理では得られない効果である。
In this case, it is important to perform a pair of ozone treatment and magnetizing treatment. This is an effect that cannot be obtained by the parallel processing of ozone treatment and magnetization treatment according to a conventional example (for example, Japanese Patent Laid-Open No. 1-262987).

【0023】さらに、磁化処理の他の効果として凝集性
について、同実験装置により簡単な検討を試みた。オゾ
ン吹き込みを中止して、供試水として蒸留水に硫酸ナト
リウム(Na2SO4)を100ppm添加し、懸濁粒子と
してカオリン(平均粒径50μm)を200ppm懸濁させ
且つ循環させながら、凝集性を検討した。その結果を図
13に示す。凝集性は任意の循環時間に沈降管に100
ミリリットル採水し、静置時間ごとに水面から10ミリ
リットルだけサンプリングして濁度を測定した。無処理
と磁化処理との濁度の差は歴然としている。磁化処理に
よる凝集性向上の理由は不明であるが、一つにカオリン
粒子のζ電位が変化していた。図14にその結果を示
す。前記実験装置で磁化処理してフラスコに循環すると
ころで循環時間ごとにサンプリングし、ジータメータ計
で分析した。通常、水中の微粒子は電気二重層を帯びて
おり、マイナス電位で、ブラウン運動により沈降しずら
い。初期のカオリン粒子のζ電位は−30〜40mVであ
るが、磁化処理しつつ循環しているとζ電位が+に転じ
るという新たな知見が得られた。このことは、PAC等
の凝集剤添加と同様の効果を意味する。したがって、オ
ゾンにより溶解性のイオンや塩類が酸化され、不溶性の
化合物として析出し、これが磁化されることにより凝集
し、分離が容易になる。これは、オゾン・磁化の直列処
理により効果が現われたものである。
Further, a simple study was made on the cohesiveness as another effect of the magnetization treatment by the same experimental apparatus. Stop ozone blowing, add 100 ppm of sodium sulfate (Na 2 SO 4 ) to distilled water as test water, suspend 200 ppm of kaolin (average particle size 50 μm) as suspended particles, and circulate while coagulating It was investigated. The result is shown in FIG. Cohesiveness is 100 in the settling tube at any circulation time.
Turbidity was measured by sampling milliliters of water and sampling only 10 milliliters from the water surface for each standing time. The difference in turbidity between untreated and magnetized is clear. Although the reason for the improvement of cohesiveness by the magnetization treatment is unknown, one of them was that the ζ potential of the kaolin particles was changed. The result is shown in FIG. Magnetization was carried out by the above-mentioned experimental apparatus, and sampling was carried out at each circulation time where it was circulated in the flask, and analyzed by a meter meter. Usually, fine particles in water have an electric double layer, and are difficult to settle due to Brownian motion at a negative potential. Although the initial ζ potential of kaolin particles is −30 to 40 mV, a new finding was obtained that the ζ potential turns to + when circulating while magnetizing. This means the same effect as adding a coagulant such as PAC. Therefore, soluble ions or salts are oxidized by ozone and precipitated as an insoluble compound, which is magnetized and agglomerated to facilitate separation. This is due to the effect of the serial treatment of ozone and magnetization.

【0024】次に、上記の実験結果から以下に本発明の
実施例を図面を用いて説明する。図1は本発明の一実施
例である高度浄水処理システムの処理フローを示す。湖
沼や河川100から着水池111に取水し、凝集剤11
0を添加して、フロック形成池112で水中の微細な浮
遊物をフロック化する。これを、凝集沈殿池113に導
き沈降分離を行い、砂ろ過池114でろ過する。ここま
では現状の上水処理プロセスと同じである。
Next, an embodiment of the present invention will be described below with reference to the drawings based on the above experimental results. FIG. 1 shows a processing flow of an advanced water purification system which is an embodiment of the present invention. The coagulant 11
0 is added to flocculate fine suspended matter in water in the floc formation pond 112. This is introduced into the coagulation sedimentation tank 113 to perform sedimentation separation, and is filtered in the sand filtration tank 114. Up to this point, it is the same as the current water treatment process.

【0025】これらに加えて、本実施例では、該ろ過水
を磁化処理装置1で処理してからオゾン反応槽2におい
て、オゾン発生機3からオゾン化空気を吹き込み、オゾ
ンで水中の異臭味等の酸化分解処理を行い、生物活性炭
塔5で浄化するようになっている。そして、浄化された
処理水は、処理水槽116で塩素115の添加によって
殺菌され、送水ポンプ117を介して水道水として給水
される。また酸化分解に供給された後の排オゾンは排オ
ゾン分解処理装置4で処理され、排気される。
In addition to these, in the present embodiment, the filtered water is treated by the magnetizing treatment apparatus 1 and then, in the ozone reaction tank 2, ozonized air is blown from the ozone generator 3 so that the ozone gives off a strange odor. Is subjected to oxidative decomposition treatment and purified in the biological activated carbon tower 5. Then, the purified treated water is sterilized by the addition of chlorine 115 in the treated water tank 116, and is supplied as tap water through the water supply pump 117. Further, the exhaust ozone after being supplied to the oxidative decomposition is processed by the exhaust ozone decomposition processing device 4 and exhausted.

【0026】なお、図1では磁化処理装置1をオゾン反
応槽2の前段に配置したが、磁化処理装置1をオゾン反
応槽2の後段に、または前段及び後段の両方に配置して
も良い。
In FIG. 1, the magnetization processing apparatus 1 is arranged in the front stage of the ozone reaction tank 2. However, the magnetization processing apparatus 1 may be arranged in the rear stage of the ozone reaction tank 2 or in both the front and rear stages.

【0027】図7は磁化処理装置の要部であり、永久磁
石式磁化処理装置の詳細を示している。また図8は磁化
処理の原理を示している。円柱型の永久磁石10を中心
にして鉄製外筒11が設けられ、磁力線10mは軸方向
に垂直に作用している。磁力線強度は600〜2000
ガウスが適当である。処理水の水流14は、配管13か
ら分配撹拌され磁石と鉄製外筒間の前記磁力線10mを
切るように通過して磁化される。このタイプは市販品に
多く、前記実験にも使用した。
FIG. 7 is a main part of the magnetization processing apparatus and shows the details of the permanent magnet type magnetization processing apparatus. FIG. 8 shows the principle of magnetization processing. An iron outer cylinder 11 is provided centering on the cylindrical permanent magnet 10, and the magnetic force lines 10m act perpendicularly to the axial direction. Magnetic field strength is 600-2000
Gauss is suitable. The water flow 14 of the treated water is distributed and agitated from the pipe 13, passes through the magnetic line of force 10 m between the magnet and the iron outer cylinder, and is magnetized. This type is common in commercial products and was used in the above experiment.

【0028】図9及び図10は電磁石式磁化処理装置の
場合を示す。流路の配管11に電磁石10aにより磁力
線を発生させる。図10は配管11内にステンレスウー
ル15を充填し、高勾配磁気分離(HGMS)の原理を
応用する、あるいはミネラル成分、例えばCa,K等を
含む砂層の充填物を設けた磁化処理の例で、流出してき
た懸濁微粒子の除去にも威力を発揮する。この場合の磁
力線強度は1000〜5000ガウスが適当である。な
お、図において10bは電磁石10aのコイルを示して
いる。
9 and 10 show the case of an electromagnet type magnetization processing device. Lines of magnetic force are generated in the pipe 11 of the flow path by the electromagnet 10a. FIG. 10 shows an example of a magnetizing process in which the stainless wool 15 is filled in the pipe 11 and the principle of high gradient magnetic separation (HGMS) is applied, or a sand layer filler containing mineral components such as Ca and K is provided. , Also effective in removing the suspended fine particles that have flowed out. In this case, the magnetic field line strength is suitably 1000 to 5000 gauss. In the figure, 10b shows a coil of the electromagnet 10a.

【0029】図2は上記した水処理システムの変形例で
ある。本変形例では、磁化処理装置1で処理した処理水
の一部を分岐させてオゾン反応槽2に導き、さらに生物
活性炭塔5で処理するようにしている。そして、生物活
性炭塔5で処理した後は、その処理水を磁化処理したま
まの水(オゾン処理装置2でオゾン処理してない水)と
合流させ、前記同様塩素殺菌してから送水ポンプ117
で給水する。本変形例によれば、オゾン反応槽2及び生
物活性炭塔5での処理水量を軽減できる。なお、図2に
おいて、磁化処理装置1の位置とオゾン処理装置2の位
置を交換し、オゾン処理した処理水の一部を磁化処理す
るようにしても、処理水量を軽減できる。
FIG. 2 shows a modification of the water treatment system described above. In this modification, a part of the treated water treated by the magnetization treatment device 1 is branched and guided to the ozone reaction tank 2 and further treated by the biological activated carbon tower 5. Then, after being treated in the biological activated carbon tower 5, the treated water is combined with the as-magnetized water (water not subjected to ozone treatment by the ozone treatment device 2) and sterilized with chlorine in the same manner as described above, and then the water pump 117.
To supply water. According to this modification, the amount of treated water in the ozone reaction tank 2 and the biological activated carbon tower 5 can be reduced. In addition, in FIG. 2, the amount of treated water can be reduced by exchanging the position of the magnetizing treatment device 1 and the position of the ozone treating device 2 and magnetizing a part of the treated water subjected to the ozone treatment.

【0030】図3も、図2と同様な変形例である。本変
形例では、磁化処理装置1で磁化処理した処理水の一部
を分岐させオゾン処理装置2でオゾン処理した後、さら
に磁化処理装置1で処理し、その後、生物活性炭槽で活
性炭処理してから、磁化処理装置1で磁化処理されたま
まの処理水と合流させ、塩素殺菌して給水する。
FIG. 3 is also a modification similar to FIG. In this modification, a part of the treated water magnetized by the magnetizing device 1 is branched and ozone-treated by the ozone treating device 2, then further treated by the magnetizing treating device 1, and then activated carbon is treated by the biological activated carbon tank. From the above, the magnetized water is merged with the treated water that has been magnetized by the magnetizing device 1, sterilized with chlorine, and water is supplied.

【0031】図4も変形例であるが、この変形例は図2
及び図3のものとは少し異なっている。すなわち、本変
形例では、磁化処理装置1で磁化処理した処理水の一部
を分岐させてオゾン反応槽2でオゾン処理し、そのオゾ
ン処理水を前記磁化処理装置1の前段に戻し、循環させ
ながら、その後に生物活性炭塔5で処理するようにして
いる。
FIG. 4 is also a modification, but this modification is shown in FIG.
And slightly different from that of FIG. That is, in this modification, a part of the treated water magnetized by the magnetizing device 1 is branched and ozone-treated in the ozone reaction tank 2, and the ozone-treated water is returned to the previous stage of the magnetizing device 1 and circulated. However, after that, the biological activated carbon tower 5 is used for treatment.

【0032】次に、図5は下水二次処理水を処理して上
水と下水の間、中水として洗車、トイレ、散水等多目的
に用いる下水二次処理水高度処理システムでの実施例を
示す。流入下水200は沈砂池210に流入し、最初沈
殿池211から曝気槽212を経て、最終沈殿池213
において下水二次処理水として塩素混和池214から放
流されるが、放流水の全量もしくは一部215aを砂ろ
過塔216でろ過し、磁化処理装置1で処理してオゾン
反応槽2でオゾン処理し、中水220として使用する。
下水二次処理水の場合、オゾン反応塔2で発泡すること
が考えられることから、消泡塔2aを経て排オゾンを排
オゾン分解処理装置4で処理して排気する。なお、21
2は下水処理水である。
Next, FIG. 5 shows an embodiment of an advanced treatment system for sewage secondary treatment water which is used for multiple purposes such as car wash, toilet and water sprinkling between the clean water and the sewage by treating the sewage secondary treatment water. Show. The inflow sewage 200 flows into the settling basin 210, passes from the first settling basin 211 through the aeration tank 212, and then to the final settling basin 213.
In chlorinated sewage, the effluent is discharged from the chlorine mixing basin 214, but all or part of the effluent 215a is filtered by the sand filter tower 216, treated by the magnetization treatment device 1 and ozone-treated in the ozone reaction tank 2. , Used as medium water 220.
In the case of sewage secondary treated water, it is considered that foaming occurs in the ozone reaction tower 2. Therefore, waste ozone is processed by the waste ozone decomposition processing device 4 and discharged through the defoaming tower 2a. In addition, 21
2 is treated sewage water.

【0033】図6はプール用水浄化システムでの実施例
を示す。プール310の水は集毛器311を経て、循環
ポンプ312でろ過塔313に送液され、磁化処理装置
1で処理され磁化処理水314としてプールへと循環す
るが、磁化処理水314の一部314aを分岐してエジ
ェクター6においてオゾン発生機3からのオゾン化空気
を取り入れオゾン反応塔2において処理され、処理水は
循環ポンプ312の吸引側に導き、循環する。オゾン反
応塔2での排オゾンは排オゾン分解処理装置4で処理し
て排気する。
FIG. 6 shows an embodiment of a pool water purification system. The water in the pool 310 passes through the hair collector 311 and is sent to the filtration tower 313 by the circulation pump 312, processed by the magnetization processing device 1 and circulated to the pool as the magnetization processed water 314. 314a is branched to take in the ozonized air from the ozone generator 3 in the ejector 6 and is treated in the ozone reaction tower 2, and the treated water is guided to the suction side of the circulation pump 312 and circulated. Exhaust ozone in the ozone reaction tower 2 is processed by the exhaust ozone decomposition processing device 4 and exhausted.

【0034】[0034]

【発明の効果】以上説明したように本発明によれば、以
下の効果がある。
As described above, the present invention has the following effects.

【0035】1)水処理システムについて 磁化とオゾン処理の相乗効果により生物活性炭塔での
浄化性能が向上し、殺菌効果が大きくなることから、塩
素添加量の削減が可能となる。
1) Water treatment system The synergistic effect of magnetization and ozone treatment improves the purification performance in the biological activated carbon tower and increases the sterilization effect, so that the amount of chlorine added can be reduced.

【0036】磁化処理水の一部をオゾン処理に分流す
ることで、オゾン処理水量が低減でき、オゾン発生機の
小型化及び消費電力の削減を達成できる。
By distributing a part of the magnetized water to the ozone treatment, the amount of the ozone treated water can be reduced, and the ozone generator can be downsized and the power consumption can be reduced.

【0037】溶解性の鉄イオンなどがオゾンにより強
力に酸化され不溶性の化合物に変化するので、それがC
a等塩類析出の核生成の芽となり凝集しても、その凝集
物の除去が容易で、水質硬度の減少が期待でき、同時に
スケール防止にも効果がある。
Since soluble iron ions are strongly oxidized by ozone and converted into insoluble compounds, it is C
Even if agglomerates are formed as nucleation buds of salt precipitation such as a, the agglomerates can be easily removed, water quality hardness can be expected to be reduced, and at the same time, scale prevention is also effective.

【0038】磁気水としての”おいしい水”が期待で
きる。
"Delicious water" as magnetic water can be expected.

【0039】永久磁石内蔵の磁化処理装置を使用する
と、新たな電力を必要とせず、コストアップとならな
い。
The use of the magnetization processing device having a built-in permanent magnet does not require new electric power and does not increase the cost.

【0040】2)下水二次処理水高度処理システムにつ
いて 磁化−オゾン処理による殺菌及び脱色により、良質の
中水が得られ、再利用水としての用途拡大が可能とな
る。
2) Sewage secondary treated water advanced treatment system By sterilization and decolorization by magnetizing-ozone treatment, good quality sewage can be obtained and its application as reused water can be expanded.

【0041】オゾン化空気の吹き込みにより、発泡成
分が同時に除去される。
The blowing component is simultaneously removed by blowing ozonized air.

【0042】3)プール用水浄化システムについて 磁化−オゾン処理水が循環するため、殺菌効果が持続
し、プールの吃水面に発生する藻類と思われる汚れ付着
がない。
3) Pool Water Purification System Since the magnetized-ozone treated water circulates, the bactericidal effect is sustained and there is no dirt adhesion which seems to be algae that is generated on the pool's water surface.

【0043】オゾン処理効果でプールの水の透明度が
高くなる。
The ozone treatment effect increases the transparency of the water in the pool.

【0044】殺菌用塩素添加量が低減でき、塩素臭が
少いため水泳時の快適性が増す。
The amount of chlorine added for sterilization can be reduced, and the smell of chlorine is small, which improves comfort during swimming.

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

【図1】本発明の水処理システムの全体構成図である。FIG. 1 is an overall configuration diagram of a water treatment system of the present invention.

【図2】図1の変形例を示した図である。FIG. 2 is a diagram showing a modification of FIG.

【図3】図1の他の変形例を示した図である。FIG. 3 is a diagram showing another modified example of FIG.

【図4】図1の更に他の変形例を示した図である。FIG. 4 is a diagram showing still another modified example of FIG.

【図5】本発明の水処理システムを適用した下水二次処
理水高度処理システムの全体構成図である。
FIG. 5 is an overall configuration diagram of a sewage secondary treated water advanced treatment system to which the water treatment system of the present invention is applied.

【図6】本発明の水処理システムを適用したプール用水
浄化処理システムの全体構成図である。
FIG. 6 is an overall configuration diagram of a pool water purification treatment system to which the water treatment system of the present invention is applied.

【図7】永久磁石式磁化処理装置の要部詳細図である。FIG. 7 is a detailed view of a main part of a permanent magnet type magnetization processing device.

【図8】磁化処理の原理を示した図である。FIG. 8 is a diagram showing a principle of magnetization processing.

【図9】電磁石式磁化処理装置の要部詳細図である。FIG. 9 is a detailed view of a main part of an electromagnet type magnetization processing device.

【図10】他の構成による電磁石式磁化処理装置の要部
詳細図である。
FIG. 10 is a detailed view of a main part of an electromagnet type magnetization processing device having another configuration.

【図11】磁化−オゾン処理の基礎実験フローを示した
図である。
FIG. 11 is a diagram showing a basic experiment flow of magnetization-ozone treatment.

【図12】磁化−オゾン処理による殺菌効果を示した図
である。
FIG. 12 is a diagram showing a bactericidal effect by magnetization-ozone treatment.

【図13】磁化処理による懸濁微粒子の凝集性を示した
図である。
FIG. 13 is a diagram showing the cohesiveness of suspended fine particles due to a magnetization treatment.

【図14】磁化処理による懸濁微粒子のζ電位の変化を
示した図である。
FIG. 14 is a diagram showing a change in ζ potential of suspended fine particles due to a magnetization process.

【符号の説明】[Explanation of symbols]

1 磁化処理装置 2 オゾン反応槽または反応塔 3 オゾン発生機 4 排オゾン分解処理装置 5 生物活性炭塔 10 永久磁石 10a 電磁石 DESCRIPTION OF SYMBOLS 1 Magnetization processing apparatus 2 Ozone reaction tank or reaction tower 3 Ozone generator 4 Waste ozone decomposition processing apparatus 5 Bioactive carbon tower 10 Permanent magnet 10a Electromagnet

───────────────────────────────────────────────────── 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 1/50 531 R 540 A 560 G (72)発明者 馬場 研二 茨城県日立市大みか町七丁目1番1号 株 式会社日立製作所日立研究所内 (72)発明者 鈴木 実 茨城県日立市国分町一丁目1番1号 株式 会社日立製作所国分工場内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification number Reference number within the agency FI Technical display location C02F 1/50 531 R 540 A 560 G (72) Inventor Kenji Baba 7-chome Omika-cho, Hitachi City, Ibaraki Prefecture No. 1-1 Hitachi Ltd., Hitachi Research Laboratory (72) Inventor Minoru Suzuki 1-1-1 Kokubuncho, Hitachi City, Ibaraki Prefecture Hitachi Ltd. Kokubun Plant

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】 処理対象水をオゾンで殺菌処理するオゾ
ン処理装置を備えた水処理システムにおいて、前記処理
対象水の中に存在する細菌類に対して磁気エネルギを与
える磁化処理装置を、処理対象水の流れに沿って前記オ
ゾン処理装置の前段又は後段の一方に、もしくは前段お
よび後段の両方に配置したことを特徴とする水処理シス
テム。
1. A water treatment system comprising an ozone treatment device for sterilizing water to be treated with ozone, wherein a magnetization treatment device for giving magnetic energy to bacteria present in the water to be treated is treated. A water treatment system characterized in that the water treatment system is arranged at one of a front stage and a rear stage of the ozone treatment device, or at both a front stage and a rear stage along the flow of water.
【請求項2】 請求項1記載の水処理システムにおい
て、前記磁化処理装置は、前記オゾン処理装置で殺菌処
理されたことにより、処理対象水の中に含まれていた溶
解性のイオン及び塩類が不溶性の化合物に、有機物が酸
化分解されて懸濁物になって析出したとき、処理対象水
を磁化処理して前記不溶性の化合物及び懸濁物を凝集さ
せることを特徴とする水処理システム。
2. The water treatment system according to claim 1, wherein the magnetization treatment device is sterilized by the ozone treatment device so that soluble ions and salts contained in the water to be treated are dissolved. A water treatment system characterized in that, when an organic substance is oxidatively decomposed into an insoluble compound and deposited as a suspension, the water to be treated is subjected to a magnetizing treatment to aggregate the insoluble compound and the suspension.
【請求項3】 処理対象水をオゾンで殺菌処理するオゾ
ン処理装置を備えた水処理システムにおいて、前記処理
対象水の中に存在する細菌類に対して磁気エネルギを与
える磁化処理装置を、処理対象水の流れに沿って前記オ
ゾン処理装置の前段に配置するとともに、前記磁化処理
装置で磁化処理した処理対象水の一部を前記オゾン処理
装置に導くことを特徴とする水処理システム。
3. A water treatment system provided with an ozone treatment device for sterilizing water to be treated with ozone, wherein a magnetizing treatment device for giving magnetic energy to bacteria present in the water to be treated is treated. A water treatment system characterized in that the water treatment system is arranged upstream of the ozone treatment device along the flow of water and guides a part of the water to be treated which has been magnetized by the magnetization treatment device to the ozone treatment device.
【請求項4】 処理対象水をオゾンで殺菌処理するオゾ
ン処理装置を備えた水処理システムにおいて、前記処理
対象水の中に存在する細菌類に対して磁気エネルギを与
える磁化処理装置を、処理対象水の流れに沿って前記オ
ゾン処理装置の後段に配置するとともに、前記オゾン処
理装置で殺菌処理した処理対象水の一部を前記磁化処理
装置に導くことを特徴とする水処理システム。
4. A water treatment system comprising an ozone treatment device for sterilizing water to be treated with ozone, wherein a magnetizing treatment device for giving magnetic energy to bacteria existing in the water to be treated is treated. A water treatment system characterized in that the water treatment system is arranged downstream of the ozone treatment device along a flow of water and guides a part of the water to be treated that has been sterilized by the ozone treatment device to the magnetization treatment device.
【請求項5】 処理対象水をオゾンで殺菌処理するオゾ
ン処理装置を備えた水処理システムにおいて、前記処理
対象水の中に存在する細菌類に対して磁気エネルギを与
える磁化処理装置を設けるとともに、前記オゾン処理装
置で殺菌処理した処理対象水の一部を磁化処理装置に導
き、前記磁化処理装置で磁化処理した処理対象水を前記
オゾン処理装置の前段側へ戻すことを特徴とする水処理
システム。
5. A water treatment system comprising an ozone treatment device for sterilizing water to be treated with ozone, wherein a magnetizing treatment device for giving magnetic energy to bacteria present in the water to be treated is provided. A water treatment system characterized in that a part of the water to be treated that has been sterilized by the ozone treatment device is guided to a magnetization treatment device, and the treatment water that has been magnetized by the magnetization treatment device is returned to the front side of the ozone treatment device. .
【請求項6】 請求項1,3〜5のいずれかに記載の水
処理システムにおいて、前記オゾン処理装置で殺菌処理
され及び前記磁化処理装置で磁化処理された処理対象水
は、後に生物活性炭で処理されることを特徴とする水処
理システム。
6. The water treatment system according to claim 1, wherein the water to be treated that has been sterilized by the ozone treatment device and magnetized by the magnetization treatment device is biological activated carbon later. A water treatment system characterized by being treated.
【請求項7】 請求項1,3〜5のいずれかに記載の水
処理システムにおいて、前記磁化処理装置は、処理対象
水に対してその流路の外側又は内側もしくは両側から磁
力線を与える磁気発生手段を有することを特徴とする水
処理システム。
7. The water treatment system according to any one of claims 1 to 3, wherein the magnetization treatment device applies magnetic lines of force to the water to be treated from outside, inside or both sides of the flow path. A water treatment system comprising means.
【請求項8】 請求項7に記載の水処理システムにおい
て、前記磁力発生手段は電磁石又は永久磁石からなり、
その磁力線強度は100〜10万ガウスに設定されてい
ることを特徴とする水処理システム。
8. The water treatment system according to claim 7, wherein the magnetic force generating means comprises an electromagnet or a permanent magnet,
The magnetic field line strength is set to 100 to 100,000 Gauss.
【請求項9】 請求項1〜8のいずれかの水処理システ
ムを用いて下水の一部を中水とする下水二次処理水高度
処理システム。
9. An advanced treatment system for sewage secondary treated water, which uses the water treatment system according to any one of claims 1 to 8 as part of sewage.
【請求項10】 請求項1〜8のいずれかの水処理シス
テムを用いてプール水を浄化するプール用水浄化システ
ム。
10. A pool water purification system for purifying pool water using the water treatment system according to claim 1.
【請求項11】 処理対象水をオゾンで殺菌処理する水
処理方法において、前記処理対象水の中に存在する細菌
類に対して磁気エネルギを与える磁化処理を、前記殺菌
処理を行う前又は後のどちらか一方で、もしくは前後の
両方で行うことを特徴とする水処理方法。
11. A water treatment method for sterilizing water to be treated with ozone, wherein a magnetizing treatment for imparting magnetic energy to bacteria present in the water to be treated is performed before or after the sterilizing treatment. A water treatment method characterized in that it is carried out either one way or both before and after.
JP33838893A 1993-12-28 1993-12-28 System and method for treating water Pending JPH07185573A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33838893A JPH07185573A (en) 1993-12-28 1993-12-28 System and method for treating water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33838893A JPH07185573A (en) 1993-12-28 1993-12-28 System and method for treating water

Publications (1)

Publication Number Publication Date
JPH07185573A true JPH07185573A (en) 1995-07-25

Family

ID=18317691

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33838893A Pending JPH07185573A (en) 1993-12-28 1993-12-28 System and method for treating water

Country Status (1)

Country Link
JP (1) JPH07185573A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997008103A1 (en) * 1995-08-23 1997-03-06 Yukiko Hayashi Water treatment method and water treatment facilities
US6030535A (en) * 1996-04-24 2000-02-29 Yukiko Hayashi Method of and apparatus for producing potable water and salt
JP2007192004A (en) * 2006-01-18 2007-08-02 Uerushii:Kk Water supply system and device utilizing underground water latent heat

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997008103A1 (en) * 1995-08-23 1997-03-06 Yukiko Hayashi Water treatment method and water treatment facilities
GB2307235A (en) * 1995-08-23 1997-05-21 Yukiko Hayashi Water treatment method and water treatment facilities
DE19680561T1 (en) * 1995-08-23 1997-09-18 Hayashi Yukiku Device and method for treating water
GB2307235B (en) * 1995-08-23 1999-06-23 Yukiko Hayashi Water treatment process and system
KR100227327B1 (en) * 1995-08-23 1999-11-01 햐야시 유키꼬 Water treatment facilities
DE19680561C2 (en) * 1995-08-23 2000-09-28 Yukiko Hayashi Water treatment device
US6030535A (en) * 1996-04-24 2000-02-29 Yukiko Hayashi Method of and apparatus for producing potable water and salt
JP2007192004A (en) * 2006-01-18 2007-08-02 Uerushii:Kk Water supply system and device utilizing underground water latent heat

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