JPH0278495A - Method and apparatus for purifying water of water supply and distribution line - Google Patents

Method and apparatus for purifying water of water supply and distribution line

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Publication number
JPH0278495A
JPH0278495A JP14848989A JP14848989A JPH0278495A JP H0278495 A JPH0278495 A JP H0278495A JP 14848989 A JP14848989 A JP 14848989A JP 14848989 A JP14848989 A JP 14848989A JP H0278495 A JPH0278495 A JP H0278495A
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JP
Japan
Prior art keywords
water
treated
electrode
electrodes
tank
Prior art date
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Application number
JP14848989A
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Japanese (ja)
Other versions
JPH0638959B2 (en
Inventor
Hideyuki Tabuchi
田淵 秀幸
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Individual
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Individual
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Publication of JPH0278495A publication Critical patent/JPH0278495A/en
Publication of JPH0638959B2 publication Critical patent/JPH0638959B2/en
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Expired - Fee Related legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

PURPOSE:To remove a mineral component in water in the form of nonadhesive scale by acting oscillating electromagnetic field to a metal salts dissolved in the water to be treated and promoting ionization of the salt by the electric oscillation energy. CONSTITUTION:HCO2 ion forms CO2 and OH ion by hydration, and CO2 is removed as gaseous CO2 out of the system by the effect of reduced pressure in a tank 2. On one hand, metal ion (mineral ion) in the water form a product having affinity with OH<-> ion which is increased in accompany with the removal of CO2 by the deaeration effect under reduced pressure in the tank 2 while the metal ion passes through a space between electrode groups A1, and deposits in the form of a product bonded to OH group. As the result, the product bonded to OH group, which is a nonadhesive deposit, is liberated and precipitated on the bottom of the tank in accompany with the promotion of ionization of the mineral component in the water, causing decrease of the mineral ion concn. in the water to be treated.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えばビル或いは工場等の給配水管や冷温水
管内の付着スケール等の原因となる水中溶存鉱物質(ミ
ネラル)を、薬品を用いることなく物理的に除去する給
配水系の水質浄化方法及び装置に関するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention is directed to the treatment of dissolved minerals in water, which cause scale build-up in water supply pipes and cold/hot water pipes in buildings or factories, for example, by treating them with chemicals. The present invention relates to a water purification method and device for water supply and distribution systems that physically removes water without using it.

〔従来の技術〕[Conventional technology]

従来における給配水管或いは冷温木管その他ボイラー冷
凍機、冷却機の水系に発生するスケールの防止対策とし
ては、イオン交換樹脂により硬水を軟水に変えるような
水の前処理方法、及び軟水を使用していても発生のみら
れるスケールに対して薬品を用いて水中の金属塩を錯体
化して処理する缶内処、理方法が広(知られている。
Conventional measures to prevent scale from occurring in the water systems of water supply and distribution pipes, cold and hot wood pipes, boilers, refrigerators, and coolers include water pretreatment methods that convert hard water into soft water using ion exchange resin, and the use of soft water. There are widely known in-can treatment methods that use chemicals to complex metal salts in the water to treat scale that can be generated even in water.

またごれらの方法以外のものとしては、静電場を有する
タンク内に水を導入し、このタンク内を減圧状態とする
ことによって水中の溶存ガスを除去すると共に、前記静
電場内の通過中に水中の未電解質のイオン解離を促進さ
せて浮遊スケールとして析出除去すると共に、水をアル
カリ性に変化させるという処理方法も知られている(特
開昭58−78003号)。
In addition, as a method other than Goret et al.'s method, water is introduced into a tank with an electrostatic field, and by reducing the pressure inside this tank, dissolved gases in the water are removed, and while passing through the electrostatic field, water is removed. A treatment method is also known in which the ion dissociation of non-electrolytes in water is promoted to remove them as floating scales, and the water is also made alkaline (Japanese Unexamined Patent Publication No. 78003/1983).

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記のように、従来では配管やボイラー等の維持管理に
際してのスケール障害を少なくする目的で、イオン交換
樹脂による水の軟化処理、酸性腐蝕防止のための脱酸剤
の投入管理、或いは固形化しているスケールに対する処
理としての清缶剤の投入管理などが行われるが、実際面
では、(1)薬品の使用は人体に有害であること、(2
)水に溶解している金属塩の量が変化するのでこれに適
切な世の薬品を投入するという管理面で困難性があると
いうこと、 (3)使い捨て薬品の量がかさむこと、などの様々な問
題点を有し、従って薬品投入を前提とした維持管理は穫
めて難しく、加えて不経済であるなどの不利益性がある
As mentioned above, in the past, in order to reduce scale damage during maintenance of pipes and boilers, water was softened using ion exchange resins, deoxidizing agents were added to prevent acid corrosion, or solidification was performed. The administration of can cleaning agents is carried out as a treatment for the scale that is present, but in reality, (1) the use of chemicals is harmful to the human body, and (2)
) The amount of metal salts dissolved in water changes, making it difficult to manage the use of appropriate chemicals; (3) The amount of disposable chemicals increases; and so on. Therefore, maintenance and management based on the injection of chemicals is extremely difficult and has disadvantages such as being uneconomical.

一方、水を静電場内で処理する方法では、水がタンク内
で電気分解を起こさないようにするために静電場を構成
する電極を信頼性のある絶縁材で被覆することを必要と
する。このことは、静電場処理系を電気回路的にコンデ
ンサーとすることであって、スイッチをONにした場合
に充電電流が流れるだけで、充電が完了すると放電され
るまで電流は流れない。
On the other hand, the method of treating water in an electrostatic field requires covering the electrodes that make up the electrostatic field with a reliable insulating material to prevent the water from electrolyzing in the tank. This means that the electrostatic field processing system is a capacitor in terms of an electric circuit, and a charging current only flows when the switch is turned on, and once charging is completed, no current flows until the capacitor is discharged.

従って静電場のみの存在となって、静電電圧を非常に高
くしないと水に付与するエネルギー効果は少ないという
欠点があった。また水の電気分解が起きない範囲で裸電
極を利用して通電処理することも考えられるが、この場
合には水中に存在するミネラルイオンの/M度に見合っ
た電流密度となるように電圧を印加することを必要とし
、このようなことは高度の電流制御システムを必要とす
ると共に電気分解を生じたときの水素の発生に対する危
険防止のうえからも制限を受けるため、実用A石面とし
て満足な効果を朋待できないという欠点があった。
Therefore, only an electrostatic field exists, and there is a drawback that unless the electrostatic voltage is extremely high, the energy effect imparted to the water is small. It is also possible to use bare electrodes to carry out current treatment within a range where water electrolysis does not occur, but in this case, the voltage should be adjusted so that the current density is commensurate with the /M degree of mineral ions present in the water. This is not satisfactory as a practical A stone surface because it requires a sophisticated current control system and is also limited by the risk prevention of hydrogen generation when electrolysis occurs. The drawback was that it was not possible to enjoy the desired effects.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は上記のような従来の浄化方法における問題点を
解決することを目的としたものであり、その基本理念は
、減圧雰囲気中での溶存ガスの脱気と被処理水中の未電
解金属塩の振動電磁界による・イオン解離の促進との組
合せ処理により被処理水中のミネラル成分を非付着スケ
ールとして析出除去する点にある。
The present invention aims to solve the problems in the conventional purification methods as described above, and its basic idea is to degas the dissolved gas in a reduced pressure atmosphere and remove unelectrolyzed metal salts from the water to be treated. Mineral components in the water to be treated are precipitated and removed as non-adhesive scale by a combination of treatment using an oscillating electromagnetic field and promotion of ion dissociation.

すなわち、本願請求項1に記載の発明に係る給配水系の
水質浄化方法では、内部を減圧状態にした処理タンク内
に被処理水を通過させて脱気すると共に、前記処理タン
クの内部で少なくとも一方が誘電体で被覆された電極対
に被処理水を接触させ、該タンク内の減圧条件により被
処理水中の溶存ガスを除去すると共に、前記電極対間に
被処理水の水質に応じて予め調整された周波数の交番電
圧を印力lすることにより前記電極対間の被処理水中の
溶存金属塩に振動電磁界を作用させ、被処理水中の金属
塩のイオン解離を電気的な振動エネルギーによって促進
させることにより非付着性の析出物として金属塩を分離
除去するものである。
That is, in the water supply and distribution system water purification method according to the invention set forth in claim 1, the water to be treated is passed through a treatment tank whose interior is in a reduced pressure state to deaerate the water, and at least Water to be treated is brought into contact with a pair of electrodes, one of which is coated with a dielectric material, and dissolved gas in the water to be treated is removed under reduced pressure conditions in the tank. By applying an alternating voltage with an adjusted frequency, an oscillating electromagnetic field is applied to the dissolved metal salt in the water to be treated between the electrode pair, and ion dissociation of the metal salt in the water to be treated is caused by electric vibrational energy. By promoting this process, metal salts are separated and removed as non-adhesive precipitates.

請求項2に記載の発明では、前記請求項1の水質浄化方
法において、前記交番電圧の周波数を、前記被処理水を
含む前記電極対間の電気回路の共振周波数に同調させる
ものである。
According to a second aspect of the invention, in the water purification method of the first aspect, the frequency of the alternating voltage is tuned to the resonance frequency of an electric circuit between the pair of electrodes containing the water to be treated.

請求項3に記載の発明では、前記請求項1の水質浄化方
法において、前記電極対に発生する磁界または電気力線
と交叉する方向に被処理水を流すものである。
According to a third aspect of the present invention, in the water purification method of the first aspect, the water to be treated is caused to flow in a direction intersecting a magnetic field or electric lines of force generated in the electrode pair.

また請求項4に記載の発明に係る給配水系の水質浄化装
置は、被処理水の導入手段と処理後の水の取出し手段と
を有する処理タンクと、処理タンク内を減圧状態に保持
して脱気する減圧脱気手段と、処理タンク内の被処理水
と接触するように配置された少なくとも一方が誘電体で
被覆された電極対と、電極対間に被処理水の水質に応じ
て予め調整された周波数の交番電圧を印加する電源装置
と、処理タンク中で被処理水中に析出した非付着性析出
物を分離除去する手段とを備えており、減圧状態の前記
タンク内に導入された被処理水を前記電極対間に連続的
に通過させる間に前記交番電圧により被処理水中の溶存
金属塩に振動電磁界エネルギーを与えるようにしたもの
である。
The water purification device for a water supply and distribution system according to the invention according to claim 4 includes a treatment tank having means for introducing water to be treated and means for taking out treated water, and maintaining the inside of the treatment tank in a reduced pressure state. A depressurizing deaeration means for degassing, an electrode pair with at least one side coated with a dielectric material and arranged so as to be in contact with the water to be treated in the treatment tank, and a It is equipped with a power supply device that applies an alternating voltage of a regulated frequency, and a means for separating and removing non-adhesive precipitates deposited in the water to be treated in the treatment tank, and is introduced into the tank in a reduced pressure state. While the water to be treated is continuously passed between the pair of electrodes, the alternating voltage applies oscillating electromagnetic field energy to the dissolved metal salts in the water to be treated.

請求項5に記載の発明では、前記請求項4の水質浄化装
置において、前記導入手段に処理タンクの上部空間に被
処理水を散水する散水手段をg(JWし、前記減圧脱気
手段に前記タンクの上部空間から脱気を行わせるように
したものである。
In the invention according to claim 5, in the water purification apparatus according to claim 4, the introducing means is provided with a water sprinkling means for sprinkling the water to be treated in the upper space of the treatment tank, and the depressurizing degassing means is provided with the The tank is degassed from the upper space.

請求項6に記載の発明では、前記請求項4の水質浄化装
置において、前記電#装置に、前記被処理水を含む前記
電極対間の電気回路の共振周波数に同調した交番電圧を
出力する可変周波数電源回路を装備したちである。
In the invention as set forth in claim 6, in the water purification apparatus as set forth in claim 4, a variable voltage is provided to output an alternating voltage tuned to a resonant frequency of an electric circuit between the pair of electrodes containing the water to be treated to the power supply device. It is equipped with a frequency power supply circuit.

請求項7に記載の発明では、前記請求項4の水質浄化装
置において、前記電極対を処理タンク内の被処理水の流
れと交叉する方向に沿って配置された複数の細長い平行
電極からなる正方格子配列電極束で構成し、被処理水が
前記電極束内の隙間を流れるようにしたものである。
In the invention as set forth in claim 7, in the water purification apparatus as set forth in claim 4, the electrode pair is a square consisting of a plurality of elongated parallel electrodes arranged along a direction intersecting the flow of the water to be treated in the treatment tank. It is composed of a bundle of electrodes in a lattice arrangement, and water to be treated flows through gaps within the electrode bundle.

更に請求項8に記載の発明では、前記請求項7の水質浄
化装置において、前記電極束の各電極に流れる電流の向
きが前記格子配列の隣接電極同士で互いに逆向きとなる
ように各電極を接続したものである。
Furthermore, in the invention according to claim 8, in the water purification apparatus according to claim 7, each electrode is arranged such that the direction of the current flowing through each electrode of the electrode bundle is opposite to that of adjacent electrodes in the lattice arrangement. It is connected.

〔作用〕[Effect]

一般に給配水系の水にはカルシウムやマグネシウムなど
の鉱物質(ミネラル)成分(金属)が、Ca (IIc
O:+) zやMg (IICO,J) 2などの炭酸
水素塩として)界在している。こ才りらのカルシウムや
マグネシウムなどの金属塩が、水中の溶存二酸化炭素の
減少や水の原発によって炭酸力ルシウムCaC0t或い
は炭酸マグネシウムMgC(hなどとして析出すると、
配管内面に強固に付着するスケールとなる。
Generally, water in water supply and distribution systems contains mineral components (metals) such as calcium and magnesium.
O: +) z and Mg (IICO, J) 2 and other hydrogen carbonates). When metal salts such as calcium and magnesium in this group are precipitated as lucium carbonate (CaC0t) or magnesium carbonate (MgC) (h) due to a decrease in dissolved carbon dioxide in water or water nuclear power generation,
It forms a scale that firmly adheres to the inner surface of the pipe.

請求項1に記載の発明に係る水質浄化方法においては、
減圧状態の処理タンク内に被処理水を導入することによ
り、水中に溶存しているCO2や02等の溶存ガスをタ
ンク内の圧力と平衡した濃度に至るまで減圧脱気してタ
ンク外に排出する。これと共にタンク内の被処理水中に
炭酸水素塩として溶存するミネラル成分が炭酸塩として
析出しないように、ミネラル成分の核外電子を外部から
の電気的な振動エネルギーによって強制的に励起させる
ことによりイオン解離させ、このミネラルイオンを被処
理水中の水酸イオンと結合させて非付着性の水酸基結合
物とするものである。
In the water purification method according to the invention according to claim 1,
By introducing the water to be treated into a treatment tank under reduced pressure, dissolved gases such as CO2 and 02 dissolved in the water are degassed under reduced pressure until the concentration is balanced with the pressure inside the tank and discharged outside the tank. do. At the same time, in order to prevent the mineral components dissolved as hydrogen carbonate in the water to be treated in the tank from precipitating as carbonates, ions are generated by forcibly exciting the extranuclear electrons of the mineral components by external electrical vibrational energy. The mineral ions are dissociated and combined with hydroxyl ions in the water to be treated to form a non-adhesive hydroxyl group-bound product.

この場合前記電気的振動エネルギーは、少なくとも一方
が誘電体で被覆された電極対の間に前記被処理水を通過
接触せしめて被処理水を含む:1ンデンサーを形成せし
め、このコンデン誉ナーの両極に交番電圧を印加するこ
とにより与える。即ち、印加された交番電圧によって電
極対間には交番電圧の周波数で振動する電磁界が生じ、
この振動電磁界の作用を受けて被処理水中のミネラル成
分の核外電子が励起され、イオン解離が促進される。
In this case, the electrical vibrational energy causes the water to be treated to pass between a pair of electrodes, at least one of which is covered with a dielectric material, to form a capacitor containing the water to be treated, and to form a condenser containing the water to be treated. This is given by applying an alternating voltage to . That is, the applied alternating voltage generates an electromagnetic field between the electrode pair that oscillates at the frequency of the alternating voltage.
Under the action of this oscillating electromagnetic field, extranuclear electrons of mineral components in the water to be treated are excited, and ion dissociation is promoted.

例えばカルシウムの場合は、被処理水中に炭酸水素塩と
して溶存するCa (HCO+) zが前記のような振
動電磁界による振動エネルギーによってカルシウムイオ
ンCa”と炭酸水素イオンlIC0,−とに解離し、更
に炭酸水素イオンが被処理水中の水と水和反応じてCO
2と水酸イオン01)−とを生しる。その他の金属炭酸
水素塩の場合も同様である。
For example, in the case of calcium, Ca (HCO+) z dissolved in the water to be treated as bicarbonate is dissociated into calcium ions Ca'' and bicarbonate ions lIC0,- by the vibration energy generated by the oscillating electromagnetic field, and further When hydrogen carbonate ions hydrate with water in the water to be treated, CO
2 and hydroxyl ion 01)-. The same applies to other metal hydrogen carbonates.

この場合、振動電磁界の振動周波数は、被処理水中のミ
ネラル成分の種類に応じて最適な振動エネルギーの授受
が行われるように予め水質測定結果などのデータにより
決定される。
In this case, the oscillation frequency of the oscillating electromagnetic field is determined in advance based on data such as water quality measurement results so that optimal vibration energy is transferred depending on the type of mineral component in the water to be treated.

このようにして電離されたミネラルイオンは被処理水中
のマイナスイオンと結合して析出物を生しるが、タンク
内は前記のように減圧されているので、被処理水中のC
CJz?a度は極めて低くなっている。従って前記ミネ
ラルイオンの多くは被処理水中で炭酸イオンと結合する
機会を失い、代りに被処理水中で増加している水酸イオ
ン01(−と親和反応を生ずることとなり、その結果、
管壁などに付着しにくい浮遊水酸化物として析出するこ
とになる。
Mineral ions ionized in this way combine with negative ions in the water to be treated to form precipitates, but since the pressure inside the tank is reduced as described above, the carbon in the water to be treated is
CJz? The a degree is extremely low. Therefore, many of the mineral ions lose the opportunity to bond with carbonate ions in the water to be treated, and instead cause an affinity reaction with the hydroxide ions 01(-) that are increasing in the water to be treated, and as a result,
It will precipitate as floating hydroxide, which is difficult to adhere to pipe walls.

この析出した水酸化状物質(水酸基結合物)、例えばC
aやMP、等は、二酸化炭素の濃度の低い被処理水中で
非付着性の水の親和物として沈澱分離され、系外へ除去
される。
This precipitated hydroxyl substance (hydroxyl group bond), for example, C
a, MP, etc. are precipitated and separated as non-adhesive water affinities in the water to be treated with a low concentration of carbon dioxide, and are removed from the system.

従ってこのような処理を経た水は、スケール発生原因と
なるミネラル成分のイオン濃度が極めて低く、また前記
水酸イオン01)−の増加によって弱いアルカリ性を呈
するので給配水系の配管などにとっても好都合である。
Therefore, water that has undergone such treatment has an extremely low ion concentration of mineral components that cause scale formation, and exhibits weak alkalinity due to the increase in hydroxyl ions, making it convenient for water supply and distribution piping. be.

ミネラル成分の析出猾は前記電極対間に印加される交番
電圧の周波数を適切に調整することにより最適に保たれ
る。このため請求項2に記載の発明では、前記交番電圧
の周、波数を、前記被処理水を含む前記電極対間の電気
回路の共振周波数に同調させる。これにより被処理水中
のミネラル成分にその種類に対応した最大の振動電磁界
エネルギーが渡され、前記イオン解離が最大効率で果た
されるようになる。
The precipitation of mineral components can be kept optimal by appropriately adjusting the frequency of the alternating voltage applied between the electrode pair. Therefore, in the invention according to claim 2, the frequency and wave number of the alternating voltage are tuned to the resonant frequency of the electric circuit between the pair of electrodes containing the water to be treated. As a result, the maximum oscillating electromagnetic field energy corresponding to the type of mineral components in the water to be treated is delivered, and the ion dissociation is carried out with maximum efficiency.

また請求項3に記載の発明において、前記電極対に発生
する磁界または電気力線と交叉する方向に被処理水を流
すと、流下する被処理水中の金属塩に対して振動電磁界
による振動作用が最も効果的に行われることになる。
Further, in the invention according to claim 3, when the water to be treated is caused to flow in a direction intersecting the magnetic field or the lines of electric force generated in the electrode pair, the oscillating electromagnetic field acts on the metal salts in the flowing water to be treated. will be done most effectively.

請求項4に記載の発明に係る給配水系の水質浄化装置は
前述請求項1に記載の発明を実施するための装置であみ
で、処理タンクは給配水系からバイパスされた被処理水
を受は入れる導入手段と処理後の水の取出し手段とを有
している。この処理タンク内の例えば上部空間は真空ポ
ンプなどを含む減圧脱気手段によって減圧状態に保持さ
れ、そこで被処理水中の溶存ガスの脱気が行われる。処
理タンク内には例えば前記上部空間の下方に溜った被処
理水中に没するように電極対が配置され、この電極対の
少なくとも一方は誘電体で被覆されたものとなっている
。電極対間には被処理水の水質に応じて予め調整された
周波数の交番電圧が電源装置から印加され、この電極対
の下方には処理タンク中で被処理水中に析出した非付着
性析出物を分離除去する例えばドレンコンクなどの手段
が設けられている。
The water purification device for a water supply and distribution system according to the invention set forth in claim 4 is an apparatus for carrying out the invention set forth in claim 1, and the treatment tank receives treated water bypassed from the water supply and distribution system. The system has an introduction means for introducing the water and a means for taking out the treated water. For example, the upper space within this treatment tank is maintained at a reduced pressure by a reduced pressure degassing means including a vacuum pump, and dissolved gas in the water to be treated is degassed there. Inside the processing tank, a pair of electrodes is arranged so as to be submerged in the water to be treated stored below the upper space, and at least one of the electrode pairs is coated with a dielectric material. An alternating voltage with a frequency pre-adjusted according to the water quality of the water to be treated is applied between the electrode pair from the power supply, and below the electrode pair, non-adhesive precipitates deposited in the water to be treated in the treatment tank are applied. For example, a means such as a drain condenser is provided to separate and remove the water.

この装置は、減圧状態の前記タンク内に導入された被処
理水を脱気しながら、タンク内で前記電極対間に連続的
に通過させる間に前記交番電圧により被処理水に振動電
磁界エネルギーを与え、これにより前記イオン解離促進
作用により被処理水中のミネラル成分をイオン化し、被
処理水中で非付着性の水酸基結合物として析出させて沈
澱等により分離し、定期的に除去するものである。
This device applies oscillating electromagnetic field energy to the water to be treated using the alternating voltage while degassing the water introduced into the tank under reduced pressure and passing it continuously between the pair of electrodes in the tank. This ionizes the mineral components in the water to be treated by the ion dissociation promoting effect, precipitates them as non-adhesive hydroxyl group-bonded substances in the water to be treated, separates them by precipitation, etc., and periodically removes them. .

請求項5に記載の発明では、前記導入手段に処理タンク
の上部空間に被処理水を散水する散水手段を装備し、被
処理水の表面積を増大させた状態にして前記減圧脱気手
段により前記タンクの上部空間から効率的に脱気を行わ
せるものである。
In the invention according to claim 5, the introduction means is equipped with a water sprinkling means for sprinkling the water to be treated in the upper space of the processing tank, and the surface area of the water to be treated is increased and the reduced pressure degassing means This allows efficient deaeration from the upper space of the tank.

請求項6に記載の発明では、前記電源装置が、前記被処
理水を含む前記電極対間の電気回路の共振周波数に同調
した交番電圧を出力する可変周波数電源回路を装備して
おり、例えば事前の水質検査などで得られたデータに基
づいて、被処理水中の溶存ミ♀ラル成分の種を刊に応し
た最大エネルギーの授受ができるようにしである。この
場合、電気的には前記回路は抵抗成分と誘導成分と容量
成分の直列共振回路であり、従ってこの回路に電源から
前記抵抗成分で定まる最大電流が流れるときの周波数を
以って共振周波数としてもよい。
In the invention according to claim 6, the power supply device is equipped with a variable frequency power supply circuit that outputs an alternating voltage tuned to a resonant frequency of an electric circuit between the pair of electrodes containing the water to be treated. Based on the data obtained from water quality tests, etc., the species of dissolved mineral components in the water to be treated is determined so that maximum energy can be given and received according to the publication. In this case, electrically, the circuit is a series resonant circuit consisting of a resistive component, an inductive component, and a capacitive component. Therefore, the resonant frequency is the frequency at which the maximum current determined by the resistive component flows from the power supply to this circuit. Good too.

請求項7に記載の発明では、前記電極対を処理タンク内
の被処理水の流れと交叉する方向に沿って配置された複
数の細長い平行電極からなる正方格子配列電極束で構成
し、被処理水が前記電極束内の隙間を流れるようにしで
ある、これば、被処理水の流れに対して乱杭のような効
果をもたせ、電極の表面積を多くして被処理水との接触
面積を増大させたものである。被処理水は電極束の間を
流れるうらに多くの電極対間を通過し、前記振動電磁界
の作用を繰返し受けることになる。
In the invention according to claim 7, the electrode pair is constituted by a square lattice array electrode bundle consisting of a plurality of elongated parallel electrodes arranged along a direction intersecting the flow of the water to be treated in the treatment tank, and The water is allowed to flow through the gaps within the electrode bundle, which creates a pile-like effect on the flow of the water to be treated, increasing the surface area of the electrodes and increasing the contact area with the water to be treated. This is what I did. In addition to flowing between the electrode bundles, the water to be treated passes between many pairs of electrodes and is repeatedly subjected to the action of the oscillating electromagnetic field.

更に請求項8に記載の発明では、前記請求項7の水質浄
化装置において、前記電極束の各電極に流れる電流の向
きが前記格子配列の隣接電極同士で互いに逆向きとなる
ように各電極を接続しである。これは、前記電極束を構
成する複数の電極のうち、電極対の一方の電極同士と他
方の電極同士とで個々に電流の折り返し経路を形成する
ように各電極端部で直列接続をなすことによって達成で
きる。このようにすると、交番電圧の印加で電極対が正
逆に充電されるときに各電極周囲に生じる交番磁束と電
気力線とがを効に被処理水と交叉するようになり、隣接
電極間で振動電磁界作用の#員失が少なくなる。
Furthermore, in the invention according to claim 8, in the water purification apparatus according to claim 7, each electrode is arranged such that the direction of the current flowing through each electrode of the electrode bundle is opposite to that of adjacent electrodes in the lattice arrangement. It is connected. This means that among the plurality of electrodes constituting the electrode bundle, the ends of each electrode are connected in series so that one electrode of the electrode pair and the other electrode form individual current return paths. This can be achieved by In this way, when an electrode pair is charged in the forward and reverse directions by applying an alternating voltage, the alternating magnetic flux and electric lines of force generated around each electrode will effectively intersect with the water to be treated, and the This reduces the loss of # members due to the action of the oscillating electromagnetic field.

本発明の好適な実施例を図面と共に説明すれば以下の通
りである。
A preferred embodiment of the present invention will be described below with reference to the drawings.

〔実施例〕〔Example〕

第1図は本発明の実施例に係る水質浄化装置の組立系統
図であり、第2図は電極群の模式構成図である。本装置
は、第1図に示すよ・うに、給水系の給水タンクlに対
して給水用接続配管4とその送水ポンプ5及び復水用接
続配管6とその復水ポンプ7をもってバイパス接続され
た処理タンク2を備えており、この処理タンク2の内部
の上部空間では気水分離器13を介して該タンクの上端
に接続された真空ポンプ3と排気管3aとによって被処
理水が減圧脱気されるようになっている。
FIG. 1 is an assembly system diagram of a water purification device according to an embodiment of the present invention, and FIG. 2 is a schematic configuration diagram of an electrode group. As shown in Fig. 1, this device is bypass-connected to the water supply tank l of the water supply system through a water supply connection pipe 4 and its water supply pump 5, and a condensate connection pipe 6 and its condensate pump 7. A treatment tank 2 is provided, and in the upper space inside the treatment tank 2, the water to be treated is degassed under reduced pressure by a vacuum pump 3 and an exhaust pipe 3a connected to the upper end of the tank via a steam separator 13. It is now possible to do so.

また前記処理タンク2内において上部空間の下方に滞留
した被処理水中には、誘電体で被覆された複数本の電極
9と、被覆されてない同本数の裸電)へ10とからなる
複数対の電極群Aが処理タンク2内に対して水平に配置
されている。この電極群Aは、第2図に示すように、前
記各々細長い電極9と裸電極10の両端が絶縁樹脂から
なるエンドプレートBによって保持されるようにして、
互いに平行に間隔をあけた正方格子配列の横架した束に
構成されている。更にこの電極群Aは、エンドプレート
Bが処理タンク2の側板2aに確実に固定されると共に
、両端のエンドプレートBの内部で電極9同士と電極1
0同士とが互いに別々に図示外のリード線等によって順
に隣接する電極と直列に結線されており、これにより隣
接電極で電流の向きが互いに逆向きとなるようになされ
ている。
In addition, in the water to be treated that has accumulated in the lower part of the upper space in the treatment tank 2, there are a plurality of electrodes 9 covered with a dielectric material and a plurality of pairs of electrodes 10, which are made up of a plurality of electrodes 9 covered with a dielectric material and the same number of bare electrodes 10 that are not covered. An electrode group A is arranged horizontally within the processing tank 2. As shown in FIG. 2, this electrode group A is constructed such that both ends of the elongated electrode 9 and the bare electrode 10 are held by an end plate B made of insulating resin.
They are arranged in horizontal bundles in a square grid array parallel to each other and spaced apart. Furthermore, in this electrode group A, the end plate B is securely fixed to the side plate 2a of the processing tank 2, and the electrodes 9 and the electrode 1 are connected to each other inside the end plates B at both ends.
0 are separately connected in series to adjacent electrodes using lead wires (not shown), so that the directions of current flow in the adjacent electrodes are opposite to each other.

前記の電極群Aには、夫々電極9と裸電極10との間に
交番電圧を印加するための電a装置12が接続されるが
、この電源装置12は、第3図に示すように、商用交流
電源から給電を受けて可変周波数の交番電源として機能
するように、フリップフロップインバータとその制御用
可変周波数発振部とを含む順逆変換装置14と、電圧増
幅部15と、電力増幅部16と、電極群Aへのインピー
ダンスマツチング用のトランス17とを具備している。
An electric power device 12 for applying an alternating voltage between the electrode 9 and the bare electrode 10 is connected to each of the electrode groups A, and as shown in FIG. A forward/reverse converter 14 including a flip-flop inverter and a variable frequency oscillator for controlling the flip-flop inverter, a voltage amplifying section 15, a power amplifying section 16 so as to receive power from a commercial AC power source and function as a variable frequency alternating power source. , and a transformer 17 for impedance matching to the electrode group A.

ここで電極対間の電気回路のインダクタンスをし、同し
く静電容量をCとすると、この回路の共振周波数r=1
/2πf丁でに等しい周波数の交番電圧を電源装置12
から印加することにより、最大効率で被処理水に振動電
磁界エネルギーを付与することができる。
If the inductance of the electric circuit between the electrode pair is C, and the capacitance is C, then the resonant frequency of this circuit is r=1
An alternating voltage with a frequency equal to /2πf is applied to the power supply 12.
By applying it from the source, it is possible to apply oscillating electromagnetic field energy to the water to be treated with maximum efficiency.

また電極群Aの各電極は、前記のような各対で直列接続
の複数の電極を正方格子配列で隣接配置して隣接電極同
士で電流の向きが逆になるようにしであるので、各電極
周囲に右ねじの法則に従って生じる磁束と各電極の半径
方向に放射状に生じる電気力線とが、隣接電極間で打ち
消されずに加算的に重なりあい、被処理水がこれら磁束
と電気力線と有効に交叉して流れることになる。
In addition, each electrode in electrode group A is constructed by arranging a plurality of series-connected electrodes in each pair adjacent to each other in a square lattice arrangement so that the direction of current is opposite between adjacent electrodes. The magnetic flux generated around the surrounding area according to the right-handed screw law and the electric lines of force generated radially in the radial direction of each electrode do not cancel out between adjacent electrodes but overlap additively, and the water to be treated interacts effectively with these magnetic flux and electric lines of force. The flow will intersect with the .

尚、処理タンク2の底部には析出して沈澱したミネラル
成分の水酸基結合物を定期的に排出するためのドレンコ
ック18が設けられている。
Incidentally, a drain cock 18 is provided at the bottom of the processing tank 2 for periodically discharging the precipitated hydroxyl-bonded mineral components.

さて、被処理水は給水タンク1から送水ポンプ5及び送
水管4を介して処理タンク2内の上部空間へ送られ、該
タンク2内に設けられた散水器8により散水状態で注入
される。処理タンク2内の水位は予め定められた高水位
HLと低水位L +−との間で電位水位計1)により検
出され、前記送水ポンプ5と、処理タンク2から給水タ
ンク1に戻る復水管6の復水ポンプ7とが自動制御され
て、処理タンク2内の平均水位が維持される。
Now, the water to be treated is sent from the water supply tank 1 to the upper space of the treatment tank 2 via the water pump 5 and the water pipe 4, and is injected in a sprinkling state by a water sprinkler 8 provided in the tank 2. The water level in the treatment tank 2 is detected between a predetermined high water level HL and a low water level L+- by the potential water level meter 1), and the water level is detected by the water pump 5 and the condensate pipe returning from the treatment tank 2 to the water supply tank 1. 6 and the condensate pump 7 are automatically controlled to maintain the average water level in the processing tank 2.

処理タンク2内に給水される水は、同タンク内の散水器
8により細かく飛散されて急に表面積が増すことになる
が、同タンク2内は前記真空ポンプ3により減圧されて
いるので、散水された水中に含まれる水素ガス及び腐蝕
性ガスをはじめC02や02などの溶存ガス及び水中に
溶解しているトリクロロエチレン等の毒性の強い揮発性
のガスなどは減圧脱気されて気水分離器13を通して槽
外に排出される。
The water supplied into the treatment tank 2 is finely scattered by the water sprinkler 8 in the tank, resulting in a sudden increase in surface area. Hydrogen gas and corrosive gases contained in the water, dissolved gases such as CO2 and 02, and highly toxic volatile gases such as trichlorethylene dissolved in the water are degassed under reduced pressure and sent to the steam-water separator 13. is discharged to the outside of the tank through the

溶存ガスが脱気された水は処理タンク2内に設けられた
電極群Aの電極9と裸電極10との間を通過するが、こ
の電極群へを通過する際に水中のミネラル成分(金属塩
)が電極対の間で前記電源装置12からの交番電圧の周
波数に応じた振動数で振動電磁界の作用を受ける。水中
に溶存する金属塩の多くばii7述したように炭酸水素
塩の形態をとっており、前記振動電磁界の作用で金属イ
オンと炭酸水素イオンとに強制的に解離される。炭酸水
素イオンは水和反応により二酸化炭素と水酸イオンOH
−とを生じ、このうち二酸化炭素CO□はタンク内の減
圧脱気作用を受けて炭酸ガスとして系外へ除去される。
Water from which dissolved gases have been degassed passes between electrode 9 and bare electrode 10 of electrode group A provided in treatment tank 2, but as it passes through this electrode group, mineral components (metals) in the water are removed. salt) is subjected to the action of an oscillating electromagnetic field between the electrode pair at a frequency corresponding to the frequency of the alternating voltage from the power supply device 12. Most of the metal salts dissolved in water are in the form of hydrogen carbonate, as described in ii7, and are forcibly dissociated into metal ions and hydrogen carbonate ions by the action of the oscillating electromagnetic field. Hydrogen carbonate ions form carbon dioxide and hydroxide ions OH through a hydration reaction.
-, of which carbon dioxide CO□ is removed from the system as carbon dioxide gas by degassing under reduced pressure inside the tank.

一方、水中の金属イオン(ミネラルイオン)は前記電極
群Aを通過する間にタンク2内の減圧脱気作用によりC
O□が除去されることに伴って増加する0■−イオンと
親和物を形成し、水酸基結合物となって析出する。この
結果、水中のミネラル成分の電離促進に伴って非付着性
析出物である水酸基結合物が遊離されてタンク底部に沈
澱し、被処理水中のミふラルイオン濃度が低下すること
となる。また、前述のように生じた水酸イオンOH−に
より被処理水は弱いアルカリ性を呈するようなる。
On the other hand, while metal ions (mineral ions) in the water pass through the electrode group A, they are degassed by the reduced pressure in the tank 2.
As O□ is removed, it forms an affinity with the 0■-ion which increases, and precipitates as a hydroxyl group bond. As a result, as the ionization of mineral components in the water is accelerated, hydroxyl-bound compounds, which are non-adhesive precipitates, are liberated and precipitate at the bottom of the tank, resulting in a decrease in the concentration of mifural ions in the water to be treated. Further, the water to be treated becomes weakly alkaline due to the hydroxyl ions OH- generated as described above.

タンク底部に沈澱した析出物はドレンコンク18を定期
的に開いて排出する。この場合、タンク下部の復水用接
続管6への出口にフィルターを設置しておくことは好ま
しいことである。
The precipitate deposited at the bottom of the tank is discharged by periodically opening the drain concavity 18. In this case, it is preferable to install a filter at the outlet to the condensate connecting pipe 6 at the bottom of the tank.

なお前記の電極群Aに印加する交番電圧の周波数は、被
処理水の水質、つまり溶存ミネラル成分の種類や量など
に応じて振動電磁界エネルギーを最大効率で作用させる
ことが望ましいので、予め被処理水の水質を確認したう
えで、電極群Aに印加する交番電圧の周波数を可変調整
し、水質に応じた適切なミネラル成分の電離を促進させ
るようにする。
Note that the frequency of the alternating voltage applied to the electrode group A is determined in advance, since it is desirable to apply the oscillating electromagnetic field energy with maximum efficiency depending on the quality of the water to be treated, that is, the type and amount of dissolved mineral components. After confirming the quality of the treated water, the frequency of the alternating voltage applied to the electrode group A is variably adjusted to promote ionization of mineral components appropriate to the water quality.

また本実施例においては電極群へが複数本の棒状電極の
束からなっているために、被処理水の水質に応じて、予
め電極群へを構成する電極9及び裸電極10の本数を組
み換えること、つまり電極9と裸電、極10との表面積
比を適宜組み換えることによってミネラル成分の電離に
対する振動電磁界エネルギーの授受を最適に調整するこ
ともできる。
Furthermore, in this embodiment, since the electrode group is made up of a bundle of multiple rod-shaped electrodes, the number of electrodes 9 and bare electrodes 10 that make up the electrode group can be rearranged in advance depending on the quality of the water to be treated. In other words, by appropriately changing the surface area ratio between the electrode 9 and the bare electrode 10, it is possible to optimally adjust the delivery and reception of oscillating electromagnetic field energy for ionization of mineral components.

更に本実施例においては、処理タンクに減圧装置や電極
群及び電源装置などを一体に付設できる構成となってい
るので、この処理タンクシステムを既設の給水タンクに
給水管及び復水管を介して接続するだけで取付は工事を
完了でき、所謂ユニット化装置として有用なシステムを
構成できるものである。
Furthermore, in this embodiment, the treatment tank is configured to be equipped with a pressure reducing device, an electrode group, a power supply device, etc., so this treatment tank system can be connected to an existing water supply tank via a water supply pipe and a condensate pipe. The installation work can be completed just by doing this, and a system useful as a so-called unitized device can be constructed.

〔発明の効果〕〔Effect of the invention〕

以上に述べたように、本発明によって水を処理する場合
には、処理タンク内をθ電圧することによって被処理水
中の溶存ガス及び地下水中に熔解している揮発性の高い
有機洗剤、例えばトリクロロエチレン等の発癌性物質を
脱気除去しつつ、振・動電磁界エネルギーにより水中に
溶解しているミネラル成分のイオン解離を促進するから
、これらミネラル成分を非付着性の水の親和物として析
出遊離することができ、処理後の水中のミネラルイオン
濃度を低下せしめてスケールのような凝集物質を生じに
くい水質浄化処理水を得ることができる。
As described above, when treating water according to the present invention, by applying a θ voltage in the treatment tank, dissolved gases in the water to be treated and highly volatile organic detergents dissolved in the groundwater, such as trichlorethylene, can be removed. While degassing and removing carcinogenic substances, the vibrational and dynamic electromagnetic field energy promotes ion dissociation of mineral components dissolved in water, so these mineral components are precipitated and released as non-adhesive water affinities. By reducing the concentration of mineral ions in the water after treatment, it is possible to obtain purified water that is less likely to produce aggregated substances such as scale.

また電極対に周波数を調整可能な交番電圧を印加するの
で、処理しようとする水の水質に応じて供給する振動電
磁界エネルギーを調整することができ、処理対象に対応
した最適処理が容易に可能である。
In addition, since an alternating voltage with adjustable frequency is applied to the electrode pair, the oscillating electromagnetic field energy supplied can be adjusted according to the quality of the water to be treated, making it easy to perform optimal treatment according to the target of treatment. It is.

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

第1図は本発明の実施例に係る水質浄化処理装置の構成
を示す組立系統図、第2図は電極群の構成を模式的に示
す斜視図、第3図は電#装置のブロック図である。 1;給水タンク、    2:処理タンク、3;真空ポ
ンプ、   3a:排気管、4:給水用接続管、   
5:送水ポンプ、6:復水用接続管、   7:復水ポ
ンプ、8:散水器、 9:電極、  10:裸電極、1
):電位水位計、 12:電Fi、装置、13:気水分
離器、 14:可変周波数順逆変l桑装置、 15;電圧増幅部、  16:電力増幅部、17:イン
ピーダンスマノチング用I・ランス、18:ドレンコソ
ク、 A:電極群、 B:絶縁材製エンドプレート。 特許用)頭人 1)淵 秀 幸 代理人弁理士 武 1)賢 曵1′、 FIG、2 日 FIG、3
Fig. 1 is an assembly system diagram showing the structure of a water purification treatment device according to an embodiment of the present invention, Fig. 2 is a perspective view schematically showing the structure of an electrode group, and Fig. 3 is a block diagram of the electrical equipment. be. 1: Water supply tank, 2: Processing tank, 3: Vacuum pump, 3a: Exhaust pipe, 4: Water supply connection pipe,
5: Water pump, 6: Condensate connection pipe, 7: Condensate pump, 8: Water sprinkler, 9: Electrode, 10: Bare electrode, 1
): Potential water level meter, 12: Electric Fi, device, 13: Steam/water separator, 14: Variable frequency forward/inverse variable l mulberry device, 15: Voltage amplification section, 16: Power amplification section, 17: Impedance manoching I/ Lance, 18: Drain pot, A: Electrode group, B: End plate made of insulating material. For patents) Head person 1) Hideyuki Fuchi Patent attorney Takeshi 1) Ken Ken 1', FIG, 2, FIG, 3

Claims (1)

【特許請求の範囲】 (1)内部を減圧状態にした処理タンク内に被処理水を
通過させて脱気すると共に、前記処理タンクの内部で少
なくとも一方が誘電体で被覆された電極対に被処理水を
接触させ、該タンク内の減圧条件により被処理水中の溶
存ガスを除去すると共に、前記電極対間に被処理水の水
質に応じて予め調整された周波数の交番電圧を印加する
ことにより前記電極対間の被処理水中の溶存金属塩に振
動電磁界を作用させ、被処理水中の金属塩のイオン解離
を電気的な振動エネルギーによって促進させることによ
り非付着性の析出物として金属塩を分離除去することを
特徴とする給配水系の水質浄化方法。 (2)前記交番電圧の周波数を、前記被処理水を含む前
記電極対間の電気回路の共振周波数に同調させることを
特徴とする請求項1に記載の水質浄化方法。 (3)前記電極対に発生する磁界または電気力線と交叉
する方向に被処理水を流すことを特徴とする請求項1に
記載の水質浄化方法。 (4)被処理水の導入手段と処理後の水の取出し手段と
を有する処理タンクと、処理タンク内を減圧状態に保持
して脱気する減圧脱気手段と、処理タンク内の被処理水
と接触するように配置された少なくとも一方が誘電体で
被覆された電極対と、電極対間に被処理水の水質に応じ
て予め調整された周波数の交番電圧を印加する電源装置
と、処理タンク中で被処理水中に析出した非付着性析出
物を分離除去する手段とを備え、減圧状態の前記タンク
内に導入された被処理水を前記電極対間に連続的に通過
させる間に前記交番電圧により被処理水中の溶存金属塩
に振動電磁界エネルギーを与えるようにしたことを特徴
とする給配水系の水質浄化装置。 (5)前記導入手段が処理タンクの上部空間に被処理水
を散水する散水手段を有し、前記減圧脱気手段が前記上
部空間から脱気を行うものである請求項4に記載の水質
浄化装置。(6)前記電源装置が、前記被処理水を含む
前記電極対間の電気回路の共振周波数に同調した交番電
圧を出力する可変周波数電源回路を有する請求項4に記
載の水質浄化装置。 (7)前記電極対が処理タンク内の被処理水の流れと交
叉する方向に沿って配置された複数の細長い平行電極か
らなる正方格子配列電極束を含み、被処理水が前記電極
束内の隙間を流れるようにした請求項4に記載の水質浄
化装置。 (8)前記電極束の各電極に流れる電流の向きが前記格
子配列の隣接電極同士で互いに逆向きとなるように各電
極を接続した請求項7に記載の水質浄化装置。
Scope of Claims: (1) The water to be treated is passed through a treatment tank whose interior is in a reduced pressure state to deaerate the water, and inside the treatment tank, the water is covered with a pair of electrodes, at least one of which is coated with a dielectric material. By contacting the treated water and removing dissolved gas in the water to be treated under reduced pressure conditions in the tank, and applying an alternating voltage with a frequency adjusted in advance depending on the quality of the water to be treated between the electrode pair. A vibrating electromagnetic field is applied to the dissolved metal salt in the water to be treated between the electrode pair, and the ion dissociation of the metal salt in the water to be treated is promoted by electric vibrational energy, thereby forming the metal salt as a non-adhesive precipitate. A water purification method for water supply and distribution systems characterized by separation and removal. (2) The water purification method according to claim 1, characterized in that the frequency of the alternating voltage is tuned to a resonance frequency of an electric circuit between the pair of electrodes containing the water to be treated. (3) The water purification method according to claim 1, characterized in that the water to be treated is caused to flow in a direction intersecting a magnetic field or electric lines of force generated in the electrode pair. (4) A treatment tank having a means for introducing water to be treated and a means for taking out water after treatment, a depressurizing degassing means for maintaining the inside of the treatment tank in a reduced pressure state and degassing it, and water to be treated in the treatment tank. a pair of electrodes, at least one of which is coated with a dielectric material, arranged to be in contact with the electrode, a power supply device that applies an alternating voltage at a frequency that is pre-adjusted depending on the quality of the water to be treated between the pair of electrodes, and a treatment tank. means for separating and removing non-adhesive precipitates precipitated in the water to be treated in the tank; A water purification device for a water supply and distribution system characterized by applying oscillating electromagnetic field energy to dissolved metal salts in water to be treated using voltage. (5) The water purification according to claim 4, wherein the introducing means has a water sprinkling means for sprinkling the water to be treated in the upper space of the treatment tank, and the depressurizing and degassing means deaerates the upper space. Device. (6) The water purification device according to claim 4, wherein the power supply device includes a variable frequency power supply circuit that outputs an alternating voltage tuned to a resonant frequency of an electric circuit between the pair of electrodes containing the water to be treated. (7) The electrode pair includes a square lattice array electrode bundle consisting of a plurality of elongated parallel electrodes arranged along a direction intersecting the flow of the water to be treated in the treatment tank, and the water to be treated is in the electrode bundle. The water purification device according to claim 4, wherein the water flows through a gap. (8) The water purification device according to claim 7, wherein the electrodes are connected so that the directions of current flowing through each electrode of the electrode bundle are opposite to each other between adjacent electrodes in the lattice arrangement.
JP14848989A 1988-06-15 1989-06-13 Water purification method and device for water supply and distribution system Expired - Fee Related JPH0638959B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP14577888 1988-06-15
JP63-145778 1988-06-15

Publications (2)

Publication Number Publication Date
JPH0278495A true JPH0278495A (en) 1990-03-19
JPH0638959B2 JPH0638959B2 (en) 1994-05-25

Family

ID=15392951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14848989A Expired - Fee Related JPH0638959B2 (en) 1988-06-15 1989-06-13 Water purification method and device for water supply and distribution system

Country Status (1)

Country Link
JP (1) JPH0638959B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102976501A (en) * 2012-10-31 2013-03-20 西安工程大学 Universal variable-frequency electromagnetic descaler and descaling method thereof
CN106927581A (en) * 2017-04-28 2017-07-07 呼延念超 A kind of temporary hardness boiler feed water corrosion-mitigation scale-inhibition water treatment system and method

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Publication number Priority date Publication date Assignee Title
JP7053929B1 (en) * 2021-07-06 2022-04-12 株式会社Ihi汎用ボイラ Water supply device and water supply method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102976501A (en) * 2012-10-31 2013-03-20 西安工程大学 Universal variable-frequency electromagnetic descaler and descaling method thereof
CN106927581A (en) * 2017-04-28 2017-07-07 呼延念超 A kind of temporary hardness boiler feed water corrosion-mitigation scale-inhibition water treatment system and method

Also Published As

Publication number Publication date
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