JP2001259691A - Method and device for preventing deposition of rust, scale and other component in fluid passage and/or removing the deposit - Google Patents

Method and device for preventing deposition of rust, scale and other component in fluid passage and/or removing the deposit

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Publication number
JP2001259691A
JP2001259691A JP2000075253A JP2000075253A JP2001259691A JP 2001259691 A JP2001259691 A JP 2001259691A JP 2000075253 A JP2000075253 A JP 2000075253A JP 2000075253 A JP2000075253 A JP 2000075253A JP 2001259691 A JP2001259691 A JP 2001259691A
Authority
JP
Japan
Prior art keywords
electric field
flow path
fluid
fluid flow
scale
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.)
Granted
Application number
JP2000075253A
Other languages
Japanese (ja)
Other versions
JP3674676B2 (en
Inventor
Shinpei Fukamachi
進平 深町
Yuichi Otani
裕一 大谷
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.)
SKA Ltd
Original Assignee
SKA 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 SKA Ltd filed Critical SKA Ltd
Priority to JP2000075253A priority Critical patent/JP3674676B2/en
Publication of JP2001259691A publication Critical patent/JP2001259691A/en
Application granted granted Critical
Publication of JP3674676B2 publication Critical patent/JP3674676B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/48Devices for applying magnetic or electric fields
    • C02F2201/483Devices for applying magnetic or electric fields using coils
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/22Eliminating or preventing deposits, scale removal, scale prevention

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method and device for making the treatment in a modulated electric field efficient, promoting its effect, investigating the cause to hinder the treatment and finding its solution. SOLUTION: A coil is wound on the surface of a first fluid passage or a second fluid passage for the fluid to be introduced into the first fluid passage to remove a cationic chemical, then a square-wave AC current with the frequency changed with time is applied on the coil, and the fluid flowing in the first fluid passage or second fluid passage is treated by a modulated electric field induced by the current flowing in the coil. Consequently, the deposition of rust, scale and other components on the wall face constituting the first fluid passage is prevented and/or the deposit is removed. This treatment in a modulated electric field is promoted by adding an anionic surfactant, sodium carbonate, sodium bicarbonate or sodium hydroxide to the water to be treated.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、流体流路を流れる
流体を変調電場処理することで、流体流路を構成する壁
面の錆び、スケール、その他の成分の付着を防止及び/
又は除去する方法と装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention prevents a rust, scale, and other components from adhering to a wall of a fluid flow path by treating a fluid flowing through the flow path with a modulated electric field.
Or a method and apparatus for removal.

【0002】[0002]

【従来の技術】従来から各種流体、例えば使用済みの工
業用水、工場排水、生活排水などの流体の流路、例えば
配管の壁面が錆びたり、スケールなどが付着して、場合
によっては流体流路が詰ってしまうことがあった。そこ
で、本発明者らは、流体流路を流れる流体を変調電場処
理することで、流体流路を構成する壁面の防錆方法、該
壁面に海生物が付着すること及び/又は除去する方法、
前記流体流路を流れる油含有排水により前記流路壁面が
詰ること等を防止する方法を開発し、特許出願(特願平
11−15192号)を行った。また、本出願人は米国
特許5,074,998号において、すでに流体流路を
流れる流体を変調電場処理することで、流体流路を構成
する壁面に付着物が付くことを防ぐ方法、該壁面に付い
た付着物を除く方法について特許を取得している。
2. Description of the Related Art Conventionally, the flow path of various fluids, for example, used industrial water, industrial wastewater, domestic wastewater, etc., for example, the wall surface of pipes is rusted or scale adheres, and in some cases, the fluid flow path Was sometimes clogged. Therefore, the present inventors, by performing a modulated electric field treatment of the fluid flowing through the fluid flow channel, a method for preventing rust on the wall surface constituting the fluid flow channel, a method for attaching and / or removing sea organisms from the wall surface,
A method for preventing the flow path wall from being clogged by oil-containing wastewater flowing through the fluid flow path was developed, and a patent application (Japanese Patent Application No. 11-15192) was filed. Further, the present applicant has disclosed in US Pat. No. 5,074,998 a method for preventing a substance attached to a wall constituting a fluid flow path by applying a modulated electric field treatment to a fluid already flowing through the fluid flow path. We have obtained a patent for a method to remove the deposits attached to.

【0003】[0003]

【発明が解決しようとする課題】前記本発明者らの特許
出願に係る発明では、流体流路を流れる流体を変調電場
処理することにより、効果的に流体流路を構成する壁面
の防錆等の処理が行われるが、流体の種類によっては目
的とする処理が十分でない場合、または目的とする処理
がほとんどできない場合があった。また、前記本発明者
らの特許出願に係る発明では、変調電場処理の効果を促
進することについては配慮がされていなかった。
In the invention according to the patent application of the present inventors, the fluid flowing through the fluid flow path is subjected to a modulated electric field treatment, thereby effectively preventing rust on the wall constituting the fluid flow path. Is performed, but depending on the type of the fluid, the desired processing may not be sufficient, or the desired processing may hardly be performed. Further, in the invention according to the patent application of the present inventors, no consideration was given to promoting the effect of the modulated electric field processing.

【0004】そこで、本発明の課題は前記本発明者らの
先の出願発明の問題点を解決し、変調電場処理を能率良
く、またその効果を促進させること及び変調電場処理を
阻害する原因を究明し、解決策を講じる方法と装置を提
供することである。
[0004] Therefore, an object of the present invention is to solve the problems of the prior application of the inventors of the present invention, to improve the efficiency of the modulation electric field processing, to promote the effect thereof, and to prevent the modulation electric field processing from being obstructed. The purpose is to provide a method and apparatus for determining and taking a solution.

【0005】[0005]

【課題を解決するための手段】本発明の上記課題は、次
の構成によって解決される。 (1)第一の流体流路または該第一の流体流路に導入す
る流体用の第二の流体流路の表面にコイルを巻きつけ、
該コイルに周波数が時間的に変化する方形波の交流電流
を流し、コイルに流れる電流により誘起される変調電場
により前記第一の流体流路又は第二の流体流路を流れる
流体を処理することにより前記第一の流体流路を構成す
る壁面の錆び、スケール、その他の成分の付着を防止及
び/又は除去する方法において、次のような処理を行
う。
The above object of the present invention is attained by the following constitution. (1) A coil is wound around the surface of the first fluid flow path or the second fluid flow path for the fluid to be introduced into the first fluid flow path,
Flowing a square wave alternating current whose frequency changes over time into the coil, and processing the fluid flowing through the first fluid flow path or the second fluid flow path by a modulated electric field induced by the current flowing through the coil. In the method for preventing and / or removing rust, scale, and other components from adhering to the wall surface constituting the first fluid flow path, the following treatment is performed.

【0006】(a)流体の前記変調電場処理を阻害する
カチオン系薬剤又はその他の前記変調電場処理阻害物質
(浮遊物質など)を除いた後に前記変調電場処理を行
う。 (b)流体の前記変調電場処理を促進するアニオン系薬
剤を添加した後に前記変調電場処理を行う。 (c)流体の前記変調電場処理を促進する炭酸ナトリウ
ム、炭酸水素ナトリウム又は水酸化ナトリウムを添加し
た後に前記変調電場処理を行う。 (d)前記(b)及び(c)の処理と共に又はこれとは
別に前記変調電場処理用の電流値などの出力を上げる。
(A) The above-mentioned modulation electric field treatment is performed after removing a cationic drug or other substances (such as suspended substances) which inhibit the above-mentioned modulation electric field treatment of a fluid. (B) performing the modulated electric field treatment after adding an anionic drug that promotes the modulated electric field treatment of the fluid; (C) performing the modulated electric field treatment after adding sodium carbonate, sodium bicarbonate or sodium hydroxide which promotes the modulated electric field treatment of the fluid; (D) The output such as the current value for the modulated electric field process is increased together with or separately from the processes (b) and (c).

【0007】次に、例えば、被処理水用配管の内壁等に
スケールが付着するメカニズムと本発明の変調電場処理
法により被処理水用配管の内壁等にスケールが付着する
ことを防止するメカニズムについて説明する。
Next, for example, a mechanism for attaching scale to the inner wall of the pipe for treated water and a mechanism for preventing the scale from adhering to the inner wall of the pipe for treated water by the modulated electric field treatment method of the present invention. explain.

【0008】まず、被処理水用配管の内壁等にスケール
が付着するメカニズムを説明する。図26に示すように
被処理水に接する配管の内壁、貯槽内壁等の表面はマイ
ナスに帯電している。被処理水中で、飽和条件下にある
スケール成分が析出して生成するスケール結晶体の表面
は、通常プラスに帯電する。この互いに異符号(プラス
とマイナス)の電位間の電気的引力によって前記内壁等
の表面にスケール成分が付着する。
First, the mechanism by which the scale adheres to the inner wall of the pipe for treated water will be described. As shown in FIG. 26, the surfaces of the inner wall of the pipe, the inner wall of the storage tank, and the like that are in contact with the water to be treated are negatively charged. The surface of the scale crystal formed by precipitation of the scale component under the saturated condition in the water to be treated is usually positively charged. The scale component adheres to the surface such as the inner wall due to the electric attraction between the potentials of opposite signs (plus and minus).

【0009】前記スケール成分は被処理水中に含まれる
無機化合物が主体であり、CaCO (炭酸カルシウ
ム)、CaSO(硫酸カルシウム)である。ただし、
単体無機化合物としてのスケール結晶体はほとんど無
く、例えばシリカスケールではSiO(シリカ)を主
体として、Ca、Mg、Al等の金属類を含み、共有結
合またはイオン結合している。また、CaCO単結合
としてのスケール結晶体は少なく、ほとんどが10〜1
00個またはそれ以上の結晶の集合体である。前記結晶
の集合体を形成する力は前述の電気的引力、又は水和力
によって生じる。
The scale component is contained in the water to be treated.
Inorganic compounds are the main components, CaCO 3(Calcium carbonate
), CaSO4(Calcium sulfate). However,
Almost no scale crystals as simple inorganic compounds
For example, in the case of silica scale, SiO2(Silica) mainly
The body contains metals such as Ca, Mg, Al, etc.
Are bonded or ionically bonded. In addition, CaCO3Single bond
As scale crystals, most of which are 10-1
It is an aggregate of 00 or more crystals. The crystal
The force that forms the aggregate is the above-mentioned electrical attraction or hydration
Caused by

【0010】また、被処理水中に溶解するCa2+、F
3+等の陽イオンの量が多いほど、同時に形成された
スケール結晶体の表面のプラス帯電力が増し、また、上
記結晶の集合体の濃度も増加してスケール成長性も高く
なる。
Further, Ca 2+ , F dissolved in the water to be treated.
As the amount of cations such as e 3+ is larger, the positive power of the surface of the scale crystal formed at the same time is increased, and the concentration of the aggregate of the crystal is also increased to increase the scale growth property.

【0011】次に、変調電場処理法により被処理水用配
管の内壁等にスケールが付着するのを防止するメカニズ
ムを図1に示す。前述のように、被処理水と接する配管
内壁、貯槽内壁等の表面はマイナスに帯電しているが、
変調電場処理された水中で形成されるスケール結晶体の
表面は、図1に示すように中性またはマイナスに帯電す
る。この同符号電位間の電気的斥力によって、反発力を
生じて、前記内壁表面などへのスケール付着を防止す
る。また、このとき、スケール結晶体同士も反発力によ
って分散し、スケール成長性を抑制し、小粒子化した結
晶が多くできやすい。
FIG. 1 shows a mechanism for preventing the scale from adhering to the inner wall or the like of the pipe for treated water by the modulated electric field treatment method. As described above, the surfaces of the pipe inner wall, the storage tank inner wall, and the like in contact with the water to be treated are negatively charged,
The surface of the scale crystal formed in the water subjected to the modulated electric field treatment is neutrally or negatively charged as shown in FIG. A repulsive force is generated by the electric repulsion between the same sign potentials, thereby preventing the scale from adhering to the inner wall surface or the like. Further, at this time, the scale crystals are also dispersed by the repulsive force, the scale growth is suppressed, and a large number of small-sized crystals are easily formed.

【0012】また、変調電場処理した水の浸透性が増加
するに伴い、スケール結晶体内部での結晶体の溶解と再
結晶化及びスケール結晶体表面のマイナス帯電による反
発力によってスケール結晶体は小粒子化され、そのため
分散されやすくなる。こうして被処理水の高流速部では
小粒子化した結晶が流下除去され易くなり、低流速部で
はそれらが沈降・堆積しやすくなる。
Further, as the permeability of the water subjected to the modulated electric field treatment increases, the scale crystal becomes smaller due to dissolution and recrystallization of the crystal inside the scale crystal and a repulsive force due to negative charge on the surface of the scale crystal. It is formed into particles, and thus easily dispersed. In this way, small-sized crystals are easily removed by flowing down in the high flow velocity portion of the water to be treated, and settle and accumulate in the low flow velocity portion.

【0013】また、硬質のスケール、例えばシリカ主体
のスケール結晶体は、そのスケール表面が平滑であれば
あるほど、変調電場処理水の浸透力を阻害させ、その軟
化及び除去に長い時間を要する。また、被処理水のpH
が低いほど、また温度が低いほど、スケール除去又はス
ケール軟化に時間がかかる。しかし、硬質のスケールで
あっても、通常の凹凸面を有するスケールの場合は、本
発明の変調電場処理で容易に軟化又は除去できるものが
多い。
Further, the harder the scale surface of the hard scale, for example, the scale crystal mainly composed of silica, the more the surface of the modulated electric field treated water is impaired, and the longer it takes to soften and remove it. The pH of the water to be treated
The lower the temperature and the lower the temperature, the longer it takes to remove or soften the scale. However, even in the case of a hard scale having a normal uneven surface, many can be easily softened or removed by the modulated electric field treatment of the present invention.

【0014】軟質スケール、例えばFe(OH)、C
a(OH)等は水和物(Fe(OH)・nHO)
としてスケールを形成し、本発明の変調電場処理水と前
記水和物内の水分子との置換が阻害され易く、スケール
除去効果が小さい。また軟質スケールが他のスライム防
止剤または防食剤として用いられるポリマー薬剤により
付着物を形成している場合も本発明の変調電場処理を阻
害しやすい。
Soft scale, for example Fe (OH) 3 , C
a (OH) 2 and the like are hydrates (Fe (OH) 3 .nH 2 O)
As a result, the displacement of the modulated electric field treated water of the present invention with the water molecules in the hydrate is easily inhibited, and the scale removing effect is small. Also, when the soft scale forms a deposit with another slime inhibitor or a polymer agent used as an anticorrosive, the modulated electric field treatment of the present invention is likely to be inhibited.

【0015】本発明の変調電場処理は好ましくは10H
z〜10MHz、より好ましくは100Hz〜1MH
z、さらに好ましくは700Hz〜3000Hzの帯域
で周波数が時間的に変化する方形波の交流電流を流すコ
イルを流体流路に巻き付けて行う。
[0015] The modulated electric field treatment of the present invention is preferably 10H
z to 10 MHz, more preferably 100 Hz to 1 MH
z, more preferably, a coil for flowing a square wave alternating current whose frequency changes with time in a band of 700 Hz to 3000 Hz is wound around the fluid flow path.

【0016】また、本発明の変調電場処理により鉄製の
装置壁面に黒錆が生成するメカニズムについて以下説明
する。本発明の変調電場処理により発生する渦電流の原
因となる誘導電場Eが図2(a)に示すように形成さ
れ、その誘導電場Eが図2(b)に示すように極大値と
なり、これが電子供与帯として還元状態となる。
The mechanism by which black rust is generated on the wall surface of the iron device by the modulated electric field treatment of the present invention will be described below. An induced electric field E causing an eddy current generated by the modulated electric field processing of the present invention is formed as shown in FIG. 2A, and the induced electric field E becomes a maximum value as shown in FIG. It becomes a reduced state as an electron donating band.

【0017】水中の溶存酸素は次式に従ってOHイオン
として働き、つぎの反応式のように黒錆が生成する。黒
錆が生成すると、以後壁面の腐食が進行しないので、黒
錆は防食作用がある。 O+2HO+4e→4OH Fe(赤錆)→Fe(黒錆) なお、本発明の変調電場処理によって帯電する箇所は水
中における水−スケール結晶、水−ガス(空気等)、水
−配管内壁等、水−油分等の界面等である。また、本発
明は上記各方法の発明を実施するための装置も含む。
The dissolved oxygen in the water acts as OH ions according to the following formula, and black rust is formed as shown in the following reaction formula. When black rust is formed, the corrosion of the wall surface does not proceed thereafter, so black rust has an anticorrosive action. O 2 + 2H 2 O + 4e - → 4OH - Fe 2 O 3 ( rust) → Fe 3 O 4 (black rust) Note that portions of charge by the modulation electric field treatment of the present invention is water in water - scale crystals, water - gas (air Etc.), water-piping inner walls, water-oil interface, etc. The present invention also includes an apparatus for carrying out the invention of each of the above methods.

【0018】本発明の変調電場処理による各種装置内で
のスケール防止、スケールの除去及び各種装置の腐食防
止、油含有排水の流路の詰まり防止、各種流体流路の壁
面への海生物付着防止等の効果を有効に作用させるため
の諸方法と、その効果確認方法について、以下に説明す
る。
Prevention of scale in various devices by the modulated electric field treatment of the present invention, removal of scale and prevention of corrosion of various devices, prevention of clogging of oil-containing drainage channels, prevention of adhesion of marine organisms to wall surfaces of various fluid channels. Various methods for making the effects such as the above effectively work and a method for confirming the effects will be described below.

【0019】本発明の変調電場処理法を実効性のあるも
のにするためには、机上試験方法で当該変調電場処理に
よる効果の確認をした上で、本発明の変調電場処理を実
機で行うことが望ましく、その実例について説明する。
In order to make the modulated electric field processing method of the present invention effective, it is necessary to confirm the effect of the modulated electric field processing by a desk test method and then to perform the modulated electric field processing of the present invention on an actual machine. Is preferable, and an example thereof will be described.

【0020】(1)未処理水 未処理水を図3に示す机上試験装置に通過させ、机上試
験装置用の被処理液を調整する。机上試験は、パイプ1
に巻いたコイル2に、経過時間に対して電流値の異なる
交流電流(出力0.14Aから25Aの間で変化、周波
数10Hz〜10MHz)を流して電磁波を変換器3で
発生させた状態で、ボトル4内の被処理水をパイプ1を
通過させることにより行う。前記机上試験装置で処理し
た被処理水をビーカ5で受け取り、その一部をガラス板
6(図4)上に滴下させて常温乾燥し、乾燥した試料の
界面部における結晶体の変化を顕微鏡で確認して、変調
電場処理効果の程度を判定する。なお、実機条件におい
て高温下である場合には前記机上試験でも実機と同一条
件となるように加温等を行い、同様の判定を行う。
(1) Untreated Water Untreated water is passed through a desk test apparatus shown in FIG. 3 to prepare a liquid to be treated for the desk test apparatus. Desk test for pipe 1
In the state in which an alternating current (an output changes from 0.14 A to 25 A, a frequency of 10 Hz to 10 MHz) having a different current value with respect to the elapsed time is passed through the coil 2, electromagnetic waves are generated by the converter 3, This is performed by passing the water to be treated in the bottle 4 through the pipe 1. The to-be-processed water treated by the desk test apparatus is received by a beaker 5, a part of which is dropped on a glass plate 6 (FIG. 4), dried at room temperature, and the change of crystal at the interface of the dried sample is observed with a microscope. After confirmation, the degree of the modulated electric field processing effect is determined. In the case of a high temperature under the actual machine conditions, heating and the like are performed in the above-mentioned desk test so that the same conditions as those of the actual machine are performed, and the same determination is performed.

【0021】(2)実機処理水 直接ガラス板上に処理水を滴下させ、常温乾燥させる。
次いで乾燥した試料の界面部での結晶体等の変化により
変調電場処理効果の判定をするのは未処理水の場合と同
様である。実機処理条件下に類似する処理により装置を
選定の上、再度、机上処理液を調整し、変調電場処理出
力不足等の確認及び変調電場処理を阻害するカチオン系
薬剤等の薬剤、浮遊物質などの不純物の残留の有無を確
認し、適切に対応した後実機で処理を再開することが必
要である。また変調電場処理出力は机上試験の結果と実
機の条件を勘案して適切な出力を設定する。
(2) Treated water in actual machine Treated water is dropped directly on a glass plate and dried at room temperature.
The determination of the effect of the modulated electric field treatment on the basis of a change in the crystal or the like at the interface of the dried sample is the same as in the case of untreated water. After selecting the equipment by similar processing under the actual processing conditions, adjust the processing liquid on the desk again, check the insufficient output of the modulated electric field processing, etc. It is necessary to check the presence or absence of impurities and to take appropriate measures to restart the processing on the actual machine. In addition, the output of the modulated electric field processing is set appropriately in consideration of the results of the desk test and the conditions of the actual machine.

【0022】本発明者らは薬剤が被処理水中に混入して
いる条件で本発明の変調電場処理を行った場合、変調電
場処理効果が発揮されなかったり、逆作用を及ぼす場合
があることについて、その原因を見いだすべく、鋭意検
討した結果、特定の薬剤が被処理水中に含まれる場合
に、被処理水の変調電場処理が阻害されることを発見し
た。また他の特定の薬剤を添加すると、被処理水の変調
電場処理が促進されることを発見した。
The present inventors consider that when the modulated electric field treatment of the present invention is performed under the condition that the drug is mixed in the water to be treated, the modulated electric field treatment effect may not be exerted or may have an adverse effect. As a result of intensive studies to find out the cause, it has been found that when a specific chemical is contained in the water to be treated, the modulated electric field treatment of the water to be treated is inhibited. It has also been discovered that the addition of other specific agents enhances the modulated electric field treatment of the water to be treated.

【0023】被処理水の変調電場処理を阻害させる薬剤
として、次のような種類のものがあった。 1.界面活性剤(カチオン系) 2.高分子剤 (カチオン系) 3.清缶剤(ボイラー) 4.スケール防止剤 5.防食剤(リン酸塩系、カチオン系高分子を含む) 6.スライム防止剤 7.帯電防止剤 8.リンス剤(乾燥仕上剤) 9.床ワックス剤 10.その他、消泡剤(シリコーン系)、海生物付着防
止剤等
There are the following types of chemicals that inhibit the modulation electric field treatment of the water to be treated. 1. Surfactant (cationic) 2. 2. Polymer agent (cationic) 3. Cleaning can (boiler) 4. Scale inhibitor 5. Anticorrosive (including phosphate and cationic polymers) 6. Slime inhibitor 7. antistatic agent 8. Rinsing agent (dry finish) Floor wax agent 10. In addition, antifoaming agents (silicone-based), marine organism adhesion inhibitor, etc.

【0024】被処理水の変調電場処理を阻害させる前記
薬剤に共通する性質を見極めることができれば、当該性
質を有する薬剤を被処理水から除去した後に変調電場処
理を行うことで、効果的に変調電場処理を行うことがで
きる。
If it is possible to determine the properties common to the above-mentioned chemicals that inhibit the modulation electric field treatment of the water to be treated, the modulation electric field treatment is carried out after removing the chemicals having the properties from the water to be treated, so that the modulation is effectively performed. Electric field treatment can be performed.

【0025】例えば、前記スライム防止剤である第四級
アンモニウム塩はプラスに帯電していることは周知のこ
とである(鈴木静夫著「冷却水の障害と処理」(株)コ
ロナ社、昭和43年発行参照)ので、前記薬剤は固体表
面電位をプラスに帯電させる「カチオン系」薬剤である
と考えられる。
For example, it is well known that the quaternary ammonium salt as the slime inhibitor is positively charged (Suzuki Shizuo, "Troubles and Treatment of Cooling Water", Corona Co., Ltd., Showa 43) Thus, the drug is considered to be a “cationic” drug that positively charges the solid surface potential.

【0026】前記カチオン系薬剤が防食剤として機能す
る場合には、次のようなメカニズムに基づくものと考え
られる。すなわち、カチオン系薬剤がマイナスに帯電す
る流体配管内壁をプラスに帯電させる共に、スケール結
晶体表面のプラス荷電力を高め、プラス(流体配管内
壁)対プラス(スケール結晶体)の反発力によって流体
配管内壁面にスケールが付着するのを防止する。また、
スケール結晶間の反発力によってスケール結晶体の成長
性も抑制する。すなわち、上記防食剤の腐食防止作用は
本発明の変調電場処理作用でスケール結晶体をマイナス
に帯電させて、マイナス帯電の流体配管内壁と反発させ
ることで防食させることとは正反対の帯電作用に基づく
ものである。
When the cationic drug functions as an anticorrosive, it is considered to be based on the following mechanism. That is, the cationic drug positively charges the inner wall of the fluid pipe, which is negatively charged, increases the positive charge power on the surface of the scale crystal, and increases the repulsive force of the plus (inner wall of the fluid pipe) to the plus (scale crystal) to the fluid pipe. Prevents the scale from adhering to the inner wall. Also,
The resilience between the scale crystals also suppresses the growth of the scale crystals. In other words, the anticorrosive action of the anticorrosive is based on the opposite charging action to anticorrosion by charging the scale crystal negatively by the modulated electric field treatment action of the present invention and repelling the inner wall of the negatively charged fluid pipe. Things.

【0027】処理対象水の変調電場処理を阻害させる薬
剤は、上記したようにメカニズムによりスケール結晶体
をプラスに帯電させる薬剤であると推定し、本発明では
これらの列挙した1.〜10.の薬剤をカチオン系薬剤
であると定義する。
It is presumed that the agent that inhibits the modulated electric field treatment of the water to be treated is an agent that positively charges the scale crystal by the mechanism as described above. -10. Is defined as a cationic drug.

【0028】従って、本発明の変調電場処理作用で流体
配管内壁面へのスケール付着及び/又は除去を図るため
には、予め前記カチオン系薬剤を除去しておくか、これ
らの薬剤注入を停止するのが有効である。ただし、製造
工程において不可欠な薬剤であり、先の3〜10の薬剤
でなければ変調電場処理装置の出力の高い機種を選定
し、先に述べた顕微鏡による机上試験による効果確認を
実施し、界面変化等良好であると判定されれば、その場
合は本発明の変調電場処理作用を阻害する薬剤の影響が
無くなったと考えられるので、そのとき条件の合致した
変調電場処理装置の出力で処理を行うことができる。
Therefore, in order to adhere and / or remove scale on the inner wall surface of the fluid pipe by the modulated electric field treatment operation of the present invention, the above-mentioned cationic drug is removed in advance or the injection of these drugs is stopped. Is effective. However, it is an indispensable chemical in the manufacturing process, and if it is not the above 3 to 10 chemicals, a model with a high output of the modulated electric field processing device is selected, and the effect is confirmed by the above-described desk test with a microscope, and the interface is checked. If it is determined that the change is favorable, in that case, it is considered that the effect of the agent that inhibits the modulated electric field processing action of the present invention has disappeared, and the processing is performed with the output of the modulated electric field processing apparatus that matches the condition at that time. be able to.

【0029】処理対象水の変調電場処理を阻害させる上
記薬剤の主なものについて、以下説明する。 1.界面活性剤 界面活性剤はカチオン性(プラス)、アニオン性(マイ
ナス)及びノニオン性界面活性剤に分別されるが、泡切
れがよい、手に着かない等のコマーシャルで、よく耳に
する洗剤の大部分はアニオン系界面活性剤であり、変調
電場処理装置への阻害作用の無いものである。皿、コッ
プ、手などは負(マイナス)に帯電しているのでアニオ
ン系洗剤を使用すると水洗いしやすい。旧世代の洗剤は
カチオン系のものであり、現在、家庭用にはほとんど使
用されなくなったが、工業用には、まだ使用していると
ころが見られる。
The main agents that inhibit the modulated electric field treatment of the water to be treated are described below. 1. Surfactants Surfactants are classified into cationic (plus), anionic (minus), and nonionic surfactants, but they are commercial products with good foam removal and inaccessibility. Most are anionic surfactants and do not have an inhibitory effect on the modulated electric field treatment device. Plates, cups, hands, etc. are negatively charged, so using an anionic detergent makes it easy to wash with water. Older generation detergents are cationic and are now rarely used for home use, but are still used for industrial purposes.

【0030】2.スケール分散剤 キレート剤、ヘキサメタリン酸ソーダなどであるが、マ
イナスに帯電する配管内壁をプラス帯電させると共に、
スケール結晶体表面のプラス荷電力を高め、プラス−プ
ラスの反発力によってスケール付着を防止する薬剤であ
る。また、スケール結晶間の反発力によって、スケール
結晶の成長性も抑制する。
2. Scale dispersant Chelating agent, sodium hexametaphosphate, etc.
It is an agent that increases the positive charge power on the scale crystal surface and prevents scale adhesion by positive-plus repulsion. In addition, the resilience between the scale crystals suppresses the growth of the scale crystals.

【0031】3.スライム防止剤 塩素剤に代表される抗菌力、また第4級アンモニウム塩
の有する殺菌力は負に帯電する細菌、藻類等に良く吸着
しやすいが、これは、スライム防止剤が正の荷電を有し
ているためである。スライム防止剤を過剰に注入する
と、その強力な酸化作用が被処理水中に残留するために
腐食障害を起こすおそれがある。
3. Slime inhibitor The antibacterial activity typified by chlorine agents and the bactericidal activity of quaternary ammonium salts are easy to adsorb to negatively charged bacteria, algae, etc., because the slime inhibitor has a positive charge. It is because. If the slime inhibitor is excessively injected, the strong oxidizing action may remain in the water to be treated and cause corrosion damage.

【0032】4.防食剤 重合リン酸塩類や高分子類等からなり、リン酸またはポ
リマー被膜を生成して、防食効果を得るものである。た
だし、過剰に注入すると、スケール防止剤中のヘキサメ
タリン酸と同様なリン酸カルシウムの生成があるだけで
なく、加水分解で生成されたリン酸イオンは細菌類の必
須栄養源となり、スライム生成による障害が生じること
もある。また、前記スライム防止剤を用いる場合、その
強い酸化力によって、鋼材腐食が促進するため、防食剤
が併用されることが多い。この場合、マイナスに帯電す
る配管内壁に被膜状に付着し、プラスに帯電させる。す
なわちプラス帯電しているスライム防止剤を配管内壁か
ら反発させることで、配管内壁の腐食防止を図るもので
ある。
4. Anticorrosives These are composed of polymerized phosphates, polymers, etc., and form a phosphoric acid or polymer film to obtain an anticorrosive effect. However, if injected excessively, not only will calcium phosphate be formed like hexametaphosphate in the scale inhibitor, but phosphate ions generated by hydrolysis will become an essential nutrient source for bacteria, causing damage by slime formation Sometimes. When the slime inhibitor is used, corrosion of steel is promoted by its strong oxidizing power, so that an anticorrosive is often used in combination. In this case, the film adheres to the inner wall of the pipe that is negatively charged in the form of a film, and is positively charged. That is, corrosion of the inner wall of the pipe is prevented by repelling the positively charged slime inhibitor from the inner wall of the pipe.

【0033】以上のように、スケール防止剤、スライム
防止剤又は防食剤などは、そのプラス帯電作用により、
その目的を達成するためのものであり、三種複合剤とし
ても用いられる場合もある。
As described above, the anti-scaling agent, anti-slime agent or anti-corrosion agent, due to its positive charging action,
This is to achieve the purpose, and may be used as a triple complex.

【0034】なお、カチオン性高分子剤が使用されてい
る設備において、本発明の変調電場処理を適用すると、
前記高分子剤の使用を停止しても残留するカチオン性高
分子剤の影響により、逆作用を生じ、配管内壁面に軟質
物質が付着し、障害を起こすおそれがある。従って、カ
チオン性高分子剤を含む被処理水に本発明の変調電場処
理を適用する場合には、装置内の被処理水をすべて入れ
替えると共に、補給水量を増加させ、残留するカチオン
性高分子剤の除去を行う必要がある。
When the modulated electric field treatment of the present invention is applied to a facility using a cationic polymer agent,
Even if the use of the polymer agent is stopped, the adverse effect may occur due to the effect of the remaining cationic polymer agent, and the soft substance may adhere to the inner wall surface of the pipe, causing a failure. Therefore, when the modulated electric field treatment of the present invention is applied to the water to be treated containing the cationic polymer agent, all the water to be treated in the device is replaced, the amount of replenishing water is increased, and the remaining cationic polymer agent is increased. Must be removed.

【0035】5.浮遊物質(SS)の影響 浮遊物質(SS)は水に不溶解性の物質であり、泥、F
e・Al系凝集ブロック、スケール結晶も含まれる。泥
などの浮遊物質(SS)は、その大部分がマイナスに帯
電しているが、Fe・Al系凝集フロック又はスケール
結晶の大部分はプラスに帯電している。
5. Influence of suspended solids (SS) Suspended solids (SS) are insoluble substances in water.
Also includes e-Al-based aggregated blocks and scale crystals. Most of suspended matter (SS) such as mud is negatively charged, but most of Fe / Al-based aggregated flocs or scale crystals are positively charged.

【0036】本発明の変調電場処理を行なった水は、プ
ラスに強く帯電している浮遊物質(SS)によってマイ
ナス帯電力が減少し、その結果、変調電場処理が済んだ
被処理水と未処理水から成る混合水のマイナス帯電力を
失う場合がある。
In the water subjected to the modulated electric field treatment of the present invention, the negative band power is reduced by the floating substance (SS) which is strongly positively charged. As a result, the water to be treated and the untreated water which have been subjected to the modulated electric field treatment are reduced. The negative power of mixed water composed of water may be lost.

【0037】さらに、プラス帯電する浮遊物質の量が3
000ppm以上であると、本発明の変調電場処理作用
が阻害される。これは浮遊物質に帯電力が消費され、未
帯電スケール結晶が残留することによるものと考えられ
る。
Further, the amount of the floating substance to be positively charged is 3
If it is 000 ppm or more, the modulated electric field treatment effect of the present invention is inhibited. This is considered to be due to the fact that the charged power is consumed by the floating substance and the uncharged scale crystals remain.

【0038】また浮遊物質がマイナスに帯電する性質を
有する場合でも、カチオン系薬剤が被処理水に多く含ま
れる場合には浮遊物質にカチオン系薬剤が付着して、全
体としてカチオン性を帯びることがある。従って、机上
試験を行い、本来マイナスに帯電している浮遊物質であ
っても、本発明の変調電場処理を適用する前に浮遊物質
を被処理水から除去することが必要な場合がある。
[0038] Even when the suspended substance has the property of being negatively charged, the cationic substance may adhere to the suspended substance when the water to be treated contains a large amount of the cationic drug, and may become cationic as a whole. is there. Therefore, it may be necessary to perform a desk test and remove the suspended substance from the water to be treated before applying the modulated electric field treatment of the present invention, even if the suspended substance is originally negatively charged.

【0039】被処理水に本発明の変調電場処理を適用す
るには、前記薬剤を含まない原水に変調電場処理を行っ
た後に、当該処理済みの原水を浮遊物質を含む被処理水
と混合すると、混合される被処理水中の浮遊物質を帯電
させる効果が高くなる。
In order to apply the modulated electric field treatment of the present invention to the water to be treated, the raw water not containing the chemical is subjected to the modulated electric field treatment, and then the treated raw water is mixed with the treated water containing the suspended substance. In addition, the effect of charging the suspended matter in the water to be mixed is increased.

【0040】本発明の変調電場処理効果を促進させる方
法として、1.アニオン系薬品との併用処理法、2.処
理炭酸ナトリウムまたは炭酸水素ナトリウムの注入法が
あることを本発明者らは発見した。
The method for promoting the effect of the modulated electric field treatment of the present invention is as follows. 1. Combination treatment method with an anionic drug; The present inventors have discovered that there is a method of injecting treated sodium carbonate or sodium bicarbonate.

【0041】1.アニオン系薬品との併用処理法 過度にプラスに帯電したスケール結晶体を形成する被処
理水に対して、本発明の変調電場処理単独では効果が出
ない場合には、アニオン系薬剤を低濃度で被処理水に注
入することで、良好な処理効果が得られる。この場合に
は、変調電場処理装置も低出力のもので対応することが
できる。
1. Combination treatment method with anionic drug For treated water that forms scale crystals that are excessively positively charged, if the modulated electric field treatment of the present invention alone has no effect, the anionic drug is used at a low concentration. By injecting into the water to be treated, a good treatment effect can be obtained. In this case, the modulation electric field processing device can also cope with a low output.

【0042】2.炭酸ナトリウムまたは炭酸水素ナトリ
ウムの注入法 カルシウムスケール障害の激しい設備においては炭酸ナ
トリウムまたは炭酸水素ナトリウム注入を併用すること
で、上記アニオン系薬剤の併用処理と同様に、変調電場
処理の効果を促進させることができる。
2. Injection method of sodium carbonate or sodium hydrogencarbonate In equipment with severe calcium scale disorder, by using sodium carbonate or sodium hydrogencarbonate injection together, promote the effect of modulated electric field treatment as well as the combined treatment of the above anionic drugs Can be.

【0043】シリカが存在することで本発明の変調電場
処理効果が得られないときには、上記薬剤の他にナトリ
ウム化合物(NaOH等)を注入することも有効であ
る。
When the effect of the modulated electric field treatment of the present invention cannot be obtained due to the presence of silica, it is also effective to inject a sodium compound (such as NaOH) in addition to the above-mentioned agents.

【0044】なお、浮遊物質を含む被処理水に前記アニ
オン系薬品又は炭酸ナトリウムまたは炭酸水素ナトリウ
ム等を添加することで、本発明の変調電場処理を適用す
る前に浮遊物質を被処理水から除去する必要がない場合
もある。
By adding the above-mentioned anionic chemical or sodium carbonate or sodium hydrogen carbonate to the water to be treated containing the suspended substance, the suspended substance is removed from the treated water before applying the modulated electric field treatment of the present invention. You may not need to.

【0045】以上、変調電場処理における配管内壁等へ
のスケールの付着防止、付着したスケールの除去及び配
管内壁等の腐食防止、油含有排水配管等の詰まり防止、
配管内壁等への海産物付着防止等の効果に対して、顕微
鏡による効果確認方法を用いることにより有効な処理方
法の選別が可能となった。
As described above, in the modulated electric field treatment, the prevention of the adhesion of scale to the inner wall of the pipe, the removal of the attached scale, the prevention of corrosion of the inner wall of the pipe, the prevention of clogging of oil-containing drainage pipe, etc.
For the effect of preventing seafood from adhering to the inner wall of pipes, etc., it became possible to select an effective treatment method by using an effect confirmation method using a microscope.

【0046】[0046]

【発明の効果】本発明によれば低コストの装置を用い
て、しかも操作性の優れた方法で流体流路を構成する壁
面が浄化され、錆び、スケール、海生物などの付着防止
及び/又は除去、配管の付着物による詰まり防止が可能
になる。
According to the present invention, the wall surface constituting the fluid flow path is purified using a low-cost apparatus and in a manner that is excellent in operability, thereby preventing rust, scale, marine organisms and the like from adhering, and / or Removal and prevention of clogging due to deposits on pipes are possible.

【0047】[0047]

【発明の実施の形態】本発明の実施の形態について図面
とともに説明する。まず、本発明の実施の形態の変調電
場処理(変調電場処理)が実際に効果があったのか確認
する机上試験方法について説明し、当該変調電場処理に
よる効果の確認をした上で、本発明の変調電場処理の実
例について説明する。
Embodiments of the present invention will be described with reference to the drawings. First, a description will be given of a desk test method for confirming whether or not the modulated electric field processing (modulated electric field processing) according to the embodiment of the present invention actually has an effect, and confirming the effect of the modulated electric field processing. An example of the modulated electric field processing will be described.

【0048】未処理水を図3に示す机上試験装置に通過
させ、机上試験装置用の被処理液を調整するが、前記机
上試験装置による試験は、パイプ1に巻いたコイル2に
経過時間に対して電流値の異なる交流電流(出力0.1
4Aから25Aの間で変化、周波数10Hz〜10MH
z)を流して電磁波を変換器3で発生させた状態で、ボ
トル4内の被処理水をパイプ1を通過させる。ビーカ5
で受けた処理水の一部をガラス板6(図4)上に滴下さ
せて常温乾燥し、図4(図4(a)は平面図、図4
(b)は側面図)に示す試料の界面部における乾燥結晶
体の変化を顕微鏡で確認して、変調電場処理効果の程度
を判定を実施する。
The untreated water is passed through a desk test apparatus shown in FIG. 3 to adjust the liquid to be treated for the desk test apparatus. In contrast, AC currents with different current values (output 0.1
Changes between 4A and 25A, frequency 10Hz-10MH
While the electromagnetic wave is generated by the converter 3 by flowing z), the water to be treated in the bottle 4 is passed through the pipe 1. Beaker 5
4 is dropped on a glass plate 6 (FIG. 4) and dried at room temperature, and FIG. 4 (FIG. 4A is a plan view, FIG.
(B) is a side view), the change of the dry crystal at the interface of the sample is confirmed with a microscope, and the degree of the modulated electric field treatment effect is determined.

【0049】マイナス帯電したスケールの結晶体の界面
付近からの反発性が最も確認される箇所はA(図4
(b))である。ただし、スケール結晶体の比重が大き
い場合、その反発力が現れにくくなる。
The location where repulsion from the vicinity of the interface of the negatively charged scale crystal is most confirmed is A (FIG. 4).
(B)). However, when the specific gravity of the scale crystal is large, the repulsive force is less likely to appear.

【0050】なお、実機条件において高温下である場合
には前記机上試験でも実機と同一条件となるように加温
等を行い、同様の判定を行う。
When the temperature is high under the actual machine conditions, heating and the like are performed in the above-mentioned desk test so that the same conditions as those of the actual machine are used, and the same judgment is made.

【0051】ここで、変調電場処理効果の程度の判定方
法は次のようにして行う。前記顕微鏡検査の結果、未処
理水と比べて次のような変化を示す場合、効果「良」と
判定する。
Here, the method of determining the degree of the modulation electric field processing effect is performed as follows. As a result of the microscopic inspection, when the following changes are shown as compared with the untreated water, the effect is determined to be “good”.

【0052】第一に小粒子結晶の生成が有ることであ
り、これは大型のスケール結晶体が変調電場処理によっ
て小粒子化及び分散性が高まったことを示す。また、第
二に界面変化があって、粒子集合性が低下し、分散性を
示すか又は粒子の反発性が有り、界面に寄っていた粒子
が変調電場処理によって界面から離れた状態を示すこと
である。さらに第三に結晶成長性が無くなり、界面を基
として、枝状に成長していた結晶体が小粒子化するか、
または枝状結晶を消失した状態を示すことである。
First, there is the formation of small grain crystals, which indicates that the large scale crystals have been made smaller and more dispersible by the modulated electric field treatment. Secondly, there is an interface change, the particle aggregation property is reduced, the dispersibility is exhibited, or the particles have resilience, and the particles close to the interface show a state separated from the interface by the modulation electric field treatment. It is. Thirdly, the crystal growth property is lost, and the crystal that has grown in a branch shape based on the interface becomes small particles,
Or, a state in which the branch crystals have disappeared.

【0053】これに対して、変調電場処理効果がないと
判定するのは、未処理水と比べて、次のような変化を示
す場合である。
On the other hand, it is determined that there is no effect of the modulated electric field treatment when there is a change as follows as compared with untreated water.

【0054】小粒子結晶の生成が無く、また前記界面で
の変化が無い場合である。この場合には、パイプ1の通
液回数を増加させると、界面付近への粒子反発性が無
く、むしろ粒子集合性を示し、結晶が成長する傾向があ
る。
This is the case where there is no generation of small particle crystals and there is no change at the interface. In this case, when the number of times of passage through the pipe 1 is increased, there is no particle resilience near the interface, but rather particles are aggregated, and crystals tend to grow.

【0055】次に本発明の変調電場処理を阻害する薬剤
を含む場合と当該薬剤を除いた場合のの変調電場処理の
結果について述べる。
Next, the results of the modulated electric field treatment in the case of including the agent which inhibits the modulated electric field treatment of the present invention and in the case of removing the agent will be described.

【0056】(1)界面活性剤 表1に各種シャンプー・リンス類を本発明の変調電場処
理の前記図3に示す机上試験を行った結果を示す。
(1) Surfactant Table 1 shows the results of the desk test shown in FIG. 3 for the modulated electric field treatment of the present invention for various shampoos and rinses.

【0057】[0057]

【表1】 [Table 1]

【0058】表1に示すように本発明の変調電場処理で
処理効果のある界面活性剤と処理効果のない界面活性剤
があるが、前述のことから本発明の変調電場処理で処理
効果のある界面活性剤(○)が負の表面電位を有するア
ニオン性の界面活性剤であり、本発明の変調電場処理で
処理効果のない界面活性剤(×)がカチオン性の表面電
位を有する界面活性剤であり、本発明の変調電場処理で
処理効果があまりない界面活性剤(△)はその極性が不
明な界面活性剤である。
As shown in Table 1, there are surfactants having a treatment effect in the modulated electric field treatment of the present invention and surfactants having no treatment effect. From the above, there is a treatment effect in the modulated electric field treatment of the present invention. The surfactant (() is an anionic surfactant having a negative surface potential, and the surfactant (×) having no treatment effect in the modulated electric field treatment of the present invention is a surfactant having a cationic surface potential. The surfactant (△), which has little treatment effect in the modulated electric field treatment of the present invention, is a surfactant whose polarity is unknown.

【0059】本発明の変調電場処理で処理効果のある界
面活性剤(○)、処理効果のない界面活性剤(×)及び
処理効果があまりない界面活性剤(△)について、机上
試験の結果を、それぞれ図5、図6及び図7の顕微鏡検
査写真に示す。
The results of the desk test of the surfactant (○) having a treatment effect in the modulated electric field treatment of the present invention, the surfactant (x) having no treatment effect, and the surfactant (△) having little treatment effect are shown. , Respectively, are shown in the micrographs of FIGS. 5, 6 and 7.

【0060】図5(×(100)15μm/目盛)は
「シャンプーE」200ppmを含む被処理水、図6
(×(100)15μm/目盛)は「ボディソープC」
100ppmを含む被処理水、図7(×(100)15
μm/目盛)は「シャンプーF」200ppmを含む被
処理水の結果である。
FIG. 5 (× (100) 15 μm / scale) shows treated water containing 200 ppm of “Shampoo E”.
(× (100) 15μm / scale) is “Body Soap C”
Water to be treated containing 100 ppm, FIG. 7 (× (100) 15
μm / scale) is the result of the water to be treated containing 200 ppm of “Shampoo F”.

【0061】図5に示す写真は界面付近に小粒子結晶が
散在していて、本発明の変調電場処理の効果が良くでて
いることを示している。一方、図6に示す写真では、界
面に大きな塊が付着していて本発明の変調電場処理効果
がないことを示している。
The photograph shown in FIG. 5 shows that small particle crystals are scattered in the vicinity of the interface, indicating that the effect of the modulated electric field treatment of the present invention is excellent. On the other hand, the photograph shown in FIG. 6 shows that a large lump adheres to the interface, and the modulated electric field treatment effect of the present invention is not present.

【0062】(2)高分子剤 変調電場処理していない冷却設備の循環水をガラス上で
乾燥させた後の顕微鏡写真を図8(a)(×(100)
15μm/目盛)に示すが、界面付近に大きな結晶体が
寄っており、スケールが生じている設備であることが分
かる。
(2) Polymer agent FIG. 8 (a) (× (100)) is a photomicrograph after circulating water of a cooling facility not subjected to a modulation electric field treatment was dried on glass.
(15 μm / scale), it can be seen that a large crystal is close to the interface, and that the scale is generated.

【0063】この循環水に本発明の机上試験を3回、5
回行った後の顕微鏡写真を撮ったが図8(b)(×(1
00)15μm/目盛)には机上試験を5回行った後の
顕微鏡写真を示す。界面にはスケール結晶体粒子の集合
性が見られる。
The circulating water was subjected to the desk test of the present invention three times,
8 (b) (× (1
(00) 15 μm / scale) shows micrographs after the desktop test was performed 5 times. Aggregation of scale crystal grains is observed at the interface.

【0064】図8(a)、図8(b)に示すように、1
回の処理での粒子の分散性を生じた状態は、3回〜5回
と処理回数を増やすと、荷電中和による凝集性を示して
いることから、カチオン系薬剤の混入が予想されたが、
この薬品は防食を目的とするカチオン系高分子物質を含
むものであることが後で判明した。
As shown in FIGS. 8A and 8B, 1
When the number of treatments was increased from 3 to 5 times, the state in which the dispersibility of the particles was caused by the number of treatments was 3 to 5 times. ,
This chemical was later found to contain a cationic polymer for corrosion protection.

【0065】このように高分子薬剤が注入されている
と、界面付近での粒子の集合性が高まっており、この被
処理水に本発明の変調電場処理を行っても効果が無いこ
とが分かる。
As described above, when the high-molecular-weight drug is injected, the aggregation property of the particles near the interface is increased, and it can be seen that the modulated electric field treatment of the present invention has no effect on the water to be treated. .

【0066】(3)清缶剤 ある市販されている特定の清缶剤を含む被処理水の変調
電場処理効果を見るために、机上試験で変調電場処理を
行った被処理水に当該清缶剤の濃度を増加させながら添
加した。その結果を図9の顕微鏡検査写真に示す。図9
(a)(×(100)15μm/目盛)は前記清缶剤1
0ppmを含む被処理水、図9(b)(×(100)1
5μm/目盛)は前記清缶剤200ppmを含む被処理
水の写真であり、薬剤注入量が増えると共に、界面付近
での粒子の集合性が高まり、本発明の変調電場処理の適
用ができないことが明らかとなった。
(3) Canned agent In order to see the effect of the modulated electric field treatment of the water to be treated containing a specific commercially available canned agent, the treated can was subjected to the modulated electric field treatment in a desk test. The agent was added in increasing concentrations. The results are shown in the micrograph of FIG. FIG.
(A) (× (100) 15 μm / scale) is the above-mentioned cleaning can 1
Water to be treated containing 0 ppm, FIG. 9 (b) (× (100) 1
(5 μm / scale) is a photograph of the water to be treated containing 200 ppm of the cleaning agent. As the injection amount of the drug increases, the collectivity of the particles near the interface increases, and the modulated electric field treatment of the present invention cannot be applied. It became clear.

【0067】(4)スケール分散剤 変調電場処理した水道水に市販されている特定のスケー
ル分散剤の濃度を種々変化させて加え、前記手順に従っ
て得た界面の顕微鏡写真を図10(a)と図10(b)
に示す。図10(a)(×(100)15μm/目盛)
はスケール防止剤50ppmを含む被処理水、図10
(b)(×(100)15μm/目盛)はスケール防止
剤200ppmを含む被処理水の写真であり、薬剤注入
量が増えると共に、界面付近での粒子の集合性が高まっ
ており、机上試験の判定方法によりカチオン系薬剤であ
ると推定した。従って、カチオン系スライム防止剤を含
む被処理水に本発明の変調電場処理を行っても効果が無
いことが分かる。
(4) Scale Dispersant A micrograph of the interface obtained according to the above procedure obtained by adding various concentrations of a specific scale dispersant commercially available to the tap water treated with the modulated electric field in various ways is shown in FIG. 10 (a). FIG. 10 (b)
Shown in FIG. 10A (× (100) 15 μm / scale)
Is the treated water containing 50 ppm of the scale inhibitor, FIG.
(B) (× (100) 15 μm / scale) is a photograph of the water to be treated containing 200 ppm of the scale inhibitor. As the amount of injected chemical increases, the collectivity of particles near the interface is increased. It was presumed to be a cationic drug by the determination method. Therefore, it can be seen that the modulated electric field treatment of the present invention does not have any effect on the water to be treated containing the cationic slime inhibitor.

【0068】(5)防食剤 特定の市販重合リン酸塩系防食剤を100ppm含む被
処理水を本発明の変調電場処理を行わないで、界面の様
子を見た顕微鏡写真が図11(×(100)15μm/
目盛)であり、本発明の変調電場処理を行った被処理水
の界面の様子を見た顕微鏡写真が図12(×(100)
15μm/目盛)であるが、この場合も、カチオン系防
食剤を含む被処理水に本発明の変調電場処理を行っても
効果が無いことが分かる。
(5) Corrosion Inhibitor FIG. 11 is a photomicrograph showing the state of the interface of treated water containing 100 ppm of a specific commercially available polymerized phosphate-based anticorrosive without subjecting to the modulated electric field treatment of the present invention. 100) 15 μm /
FIG. 12 (× (100)) is a micrograph showing the state of the interface of the water to be treated which has been subjected to the modulated electric field treatment of the present invention.
(15 μm / scale), but also in this case, it can be seen that the modulated electric field treatment of the present invention on the water to be treated containing the cationic anticorrosive has no effect.

【0069】(6)スライム防止剤 変調電場処理した水道水に特定の市販スライム防止剤の
濃度を種々変化させて加え、前記手順に従って得た界面
の顕微鏡写真を図13(a)と図13(b)に示す。図
13(a)(×(100)15μm/目盛)はスライム
防止剤10ppmを含む被処理水、図13(b)(×
(100)15μm/目盛)はスライム防止剤200p
pmを含む被処理水の写真であり、薬剤注入量が増える
と共に、界面付近での粒子の集合性が高まっており、机
上試験の判定方法によりカチオン系薬剤であると推定し
た。この場合も、カチオン系スライム防止剤を含む被処
理水に本発明の変調電場処理を行っても効果が無いこと
が分かる。
(6) Slime Preventive Agent A microphotograph of the interface obtained according to the above procedure was added to the tap water treated with the modulated electric field while changing the concentration of the specific commercial slime preventive agent in various ways, and FIG. It is shown in b). FIG. 13 (a) (× (100) 15 μm / scale) is the treated water containing 10 ppm of the slime inhibitor, and FIG. 13 (b) (×
(100) 15 μm / scale) is 200 slime inhibitor
This is a photograph of the water to be treated including pm, and as the amount of injected drug increases, the collectability of particles near the interface increases, and it was estimated that the product was a cationic drug by the determination method of the desk test. Also in this case, it can be seen that the modulated electric field treatment of the present invention does not have any effect on the water to be treated containing the cationic slime inhibitor.

【0070】(7)帯電防止剤 変調電場処理した被処理水に特定の市販帯電防止剤の濃
度を種々変化させて加え、前記手順に従って得た界面の
顕微鏡写真を図14(a)と図14(b)に示す。図1
4(a)(×(100)15μm/目盛)は帯電防止剤
と界面活性剤を10ppmを含む被処理水、図14
(b)(×(100)15μm/目盛)は帯電防止剤と
界面活性剤を200ppmを含む被処理水の写真であ
り、薬剤注入量が増えると共に、界面付近での粒子の集
合性が高まっており、机上試験の判定方法によりカチオ
ン系薬剤であると推定した。この場合も、カチオン系ス
ライム防止剤を含む被処理水に本発明の変調電場処理を
行っても効果が無いことが分かる。
(7) Antistatic Agent A microphotograph of the interface obtained according to the above procedure was added to the water to be treated subjected to the modulated electric field treatment while varying the concentration of the specific commercially available antistatic agent. (B). FIG.
4 (a) (× (100) 15 μm / scale) is treated water containing 10 ppm of an antistatic agent and a surfactant, FIG.
(B) (× (100) 15 μm / scale) is a photograph of the water to be treated containing 200 ppm of an antistatic agent and a surfactant. As the amount of injected medicine increases, the aggregation of particles near the interface increases. Therefore, it was presumed to be a cationic drug by the determination method of the desk test. Also in this case, it can be seen that the modulated electric field treatment of the present invention does not have any effect on the water to be treated containing the cationic slime inhibitor.

【0071】(8)リンス剤 変調電場処理した被処理水に特定の市販されているリン
ス剤の濃度を種々変化させて加え、前記手順に従って得
た界面の顕微鏡写真を図15(a)と図15(b)に示
す。図15(a)(×(100)15μm/目盛)はリ
ンス剤50ppmを含む被処理水、図15(b)(×
(100)15μm/目盛)はリンス防止剤200pp
mを含む被処理水の写真であり、薬剤注入量が増えると
共に、界面付近での粒子の集合性が高まっており、机上
試験の判定方法によりカチオン系薬剤であると推定し
た。この場合も、リンス剤を含む被処理水に本発明の変
調電場処理を行っても効果が無いことが分かる。
(8) Rinse Agent A micrograph of the interface obtained according to the above procedure was added to the water to be treated subjected to the modulated electric field treatment while varying the concentration of a specific commercially available rinse agent, and FIG. This is shown in FIG. 15 (a) (× (100) 15 μm / scale) is the water to be treated containing 50 ppm of the rinsing agent, and FIG. 15 (b) (×
(100) 15 μm / scale) is a rinse inhibitor 200 pp
This is a photograph of the water to be treated containing m, which shows that the amount of drug injected increased and the aggregation of particles near the interface increased, and it was presumed to be a cationic drug by the determination method of the desk test. Also in this case, it can be seen that the modulated electric field treatment of the present invention on the water to be treated containing the rinsing agent has no effect.

【0072】(9)海生物付着防止剤 変調電場処理した被処理水に特定の市販海生物付着防止
剤の濃度を種々変化させて加え、前記手順に従って机上
試験を行い、界面の顕微鏡写真を図16(a)と図16
(b)に示す。図16(a)(×(100)15μm/
目盛)は海生物付着防止剤50ppmを含む被処理水、
図16(b)(×(100)15μm/目盛)は海生物
付着防止剤200ppmを含む被処理水の写真であり、
薬剤注入量が増えると共に、界面付近での粒子の集合性
が高まっており、机上試験の判定方法によりカチオン系
薬剤であると推定した。この場合も、海生物付着防止剤
を含む被処理水に本発明の変調電場処理を行っても効果
が無いことが分かる。
(9) Sea Life Antifouling Agent The concentration of the specific commercially available sea life antifouling agent was varied and added to the treated water subjected to the modulated electric field treatment, and a desk test was conducted in accordance with the above procedure. 16 (a) and FIG.
(B). FIG. 16 (a) (× (100) 15 μm /
Scale) is water to be treated containing 50 ppm of a marine organism adhesion inhibitor,
FIG. 16B (× (100) 15 μm / scale) is a photograph of the water to be treated containing 200 ppm of the marine organism adhesion inhibitor,
As the drug injection amount increased, the collectability of particles near the interface increased, and it was presumed to be a cationic drug by the determination method of the desk test. Also in this case, it can be seen that there is no effect even if the modulated electric field treatment of the present invention is performed on the water to be treated containing the marine organism adhesion inhibitor.

【0073】(10)防食剤(重合リン酸塩)を含む被
処理水に本発明の変調電場処理法を適用した例 発電所設備の軸受け冷却水のサンプリングラックを長期
間使用中にスケールが付着するので、その対策として本
発明の変調電場処理を適用した。
(10) An example in which the modulated electric field treatment method of the present invention is applied to water to be treated containing an anticorrosive (polymerized phosphate) Scale adheres during long-term use of the bearing cooling water sampling rack of power plant equipment Therefore, the modulation electric field processing of the present invention was applied as a countermeasure.

【0074】図17には発電所設備の軸受け冷却水の循
環系を示す。冷却水タンク10には薬品注入設備11か
ら随時防食剤(重合リン酸塩)が注入され、また工業用
水も補給される。冷却水タンク10からは熱交換装置1
2の軸受けに冷却水が循環供給されるが、当該熱交換装
置12の軸受け部分の冷却水は複数並列設置されている
サンプリングラック13を経由した冷却水タンク10に
戻る。
FIG. 17 shows a circulating system of the bearing cooling water of the power plant equipment. An anticorrosive (polymerized phosphate) is injected into the cooling water tank 10 from the chemical injection equipment 11 as needed, and industrial water is also supplied. From the cooling water tank 10, the heat exchange device 1
Although the cooling water is circulated and supplied to the second bearing, the cooling water in the bearing portion of the heat exchange device 12 returns to the cooling water tank 10 via the sampling racks 13 installed in parallel.

【0075】本発明の変調電場処理装置14はサンプリ
ングラック13への導入部の各循環冷却水配管15に設
けられる。そして変調電場処理水を冷却水タンク10に
流入させるが、このとき、薬品注入設備11から防食剤
(重合リン酸塩)を添加した。
The modulated electric field processing device 14 of the present invention is provided in each circulating cooling water pipe 15 of the introduction part to the sampling rack 13. Then, the modulated electric field treated water was allowed to flow into the cooling water tank 10, and at this time, an anticorrosive (polymerized phosphate) was added from the chemical injection facility 11.

【0076】図18(a)にはサンプリングラック13
の冷却器の外側にスケールが付着した状況を示す。図1
8(b)には本発明の変調電場処理14を4ヶ月間連続
して行った後のサンプリングラック13の冷却器の外側
のスケールの状態を示す。
FIG. 18A shows the sampling rack 13.
Shows the situation where scale adhered to the outside of the cooler. FIG.
FIG. 8B shows the state of the scale outside the cooler of the sampling rack 13 after performing the modulated electric field treatment 14 of the present invention continuously for four months.

【0077】被処理水にカチオン系の防食剤(重合リン
酸塩)が含まれたままで変調電場処理したため、スケー
ルは軟質化しているが、冷却器に付着したままであり、
スケール除去効果が十分ではない。
Since the modulated electric field treatment was performed with the water to be treated containing the cationic anticorrosive (polymerized phosphate), the scale was softened, but remained attached to the cooler.
The scale removal effect is not sufficient.

【0078】また図19(a)には本発明の変調電場処
理をする前の前記サンプリングラック13の冷却器を収
納しているケースにスケールが多く付着している状態を
示す写真である。図19(b)には防食剤(重合リン酸
塩)を含む被処理水を本発明の変調電場処理装置14で
4ヶ月間連続して処理を行った後の前記ケーシングの内
壁面を示すが、赤錆表面の軟質化と、黒錆が多く形成さ
れていることが確認された。
FIG. 19 (a) is a photograph showing a state in which a large amount of scale is attached to the case housing the cooler of the sampling rack 13 before performing the modulated electric field treatment of the present invention. FIG. 19B shows the inner wall surface of the casing after the water to be treated containing the anticorrosive (polymerized phosphate) has been continuously treated by the modulated electric field treatment device 14 for four months. It was confirmed that the surface of the red rust was softened and a large amount of black rust was formed.

【0079】(11)懸濁物質(SS)を含む被処理水
に本発明の変調電場処理法を適用した例 図20に示すディーゼル発電機の開放型冷却設備の二次
冷却水の循環流路に本発明の変調電場処理を適用した。
図20で熱交換器17から排出する二次冷却水は開放型
冷却塔18で冷却されてポンプ19とストレーナ20を
介して再び熱交換器に戻される。この実機の二次冷却水
の循環流路に本発明の変調電場処理装置14を適用する
に先立ち、この二次冷却水の循環流路の壁面にスケール
が付着することを防止するために使用されるスライム防
止剤及びスケール分散剤を二次冷却水に添加してある場
合に本発明の変調電場処理が効果的か否か確認する机上
試験を行った。
(11) An example in which the modulated electric field treatment method of the present invention is applied to the water to be treated containing the suspended solid (SS) The circulation flow path of the secondary cooling water of the open-type cooling facility of the diesel generator shown in FIG. The modulated electric field processing of the present invention was applied to the present invention.
In FIG. 20, the secondary cooling water discharged from the heat exchanger 17 is cooled in the open type cooling tower 18 and returned to the heat exchanger again via the pump 19 and the strainer 20. Prior to applying the modulated electric field treatment device 14 of the present invention to the circulation path of the secondary cooling water of the actual machine, it is used to prevent scale from adhering to the wall surface of the circulation path of the secondary cooling water. A desk test was conducted to confirm whether the modulated electric field treatment of the present invention was effective when a slime inhibitor and a scale dispersant were added to the secondary cooling water.

【0080】変調電場処理した水道水に特定の市販スラ
イム防止剤とスケール防止剤の濃度を10、50、10
0、200ppmと変化させて加え、前記手順に従って
得た界面の顕微鏡写真の代表例を図21(a)と図21
(b)にそれぞれ示す。図21(a)(×(100)1
5μm/目盛)はスライム防止剤100ppmを含む被
処理水、図21(b)(×(100)15μm/目盛)
はスケール防止剤100ppmを含む被処理水の写真を
示すが、薬剤注入量が増えると共に、界面付近での粒子
の集合性と結晶成長性が高まっていることが分かる。
The concentration of the specific commercial slime inhibitor and scale inhibitor was added to the tap water treated with the modulated electric field by 10, 50, 10
FIGS. 21 (a) and 21 (a) show typical examples of micrographs of the interface obtained according to the above-mentioned procedure while changing the amounts to 0 and 200 ppm.
(B) shows each. FIG. 21 (a) (× (100) 1
(5 μm / scale) is treated water containing 100 ppm of a slime inhibitor, FIG. 21 (b) (× (100) 15 μm / scale)
Shows a photograph of water to be treated containing 100 ppm of a scale inhibitor. It can be seen that as the chemical injection amount increases, the collectivity and crystal growth of particles near the interface increase.

【0081】そして、図20に示す開放型冷却塔18の
底部に残留していた乳白色ポリマー状の物質を採取し、
顕微鏡検査を実施した結果を図22に示す。図22に示
す界面上にスケール成分が集合しているが、これは、ス
ケール分散剤を含む懸濁物質であることが分かる。
Then, a milky white polymer-like substance remaining at the bottom of the open type cooling tower 18 shown in FIG.
The results of the microscopic inspection are shown in FIG. Scale components are aggregated on the interface shown in FIG. 22, and it is understood that this is a suspended substance containing a scale dispersant.

【0082】そして図23はスケール分散剤を含む懸濁
物質を除去する前に熱交換器17でのスケールが付着し
た状況を示す写真(特に配管の上半分にスケールが多く
付着している)である。しかしストレーナ20を設置し
て懸濁物質を除去した後に本発明の変調電場処理装置1
4を適用した所、図24に示すように熱交換器17はき
れいになりスケール付着物が全く無かった。
FIG. 23 is a photograph showing the situation where the scale adhered to the heat exchanger 17 before removing the suspended substance containing the scale dispersant (particularly, a large amount of the scale adhered to the upper half of the pipe). is there. However, after installing the strainer 20 to remove suspended substances, the modulated electric field processing apparatus 1 of the present invention is used.
When No. 4 was applied, as shown in FIG. 24, the heat exchanger 17 was clean and had no scale deposits.

【0083】次に変調電場処理を促進させる実施の形態
について述べる。地熱発電設備への本発明の変調電場処
理装置を適用した場合について、補助薬剤(炭酸水素ナ
トリウム)との併用で変調電場処理装置単独での処理以
上の効果が得られるかどうか、机上試験を行った。前記
手順に従って得た界面の顕微鏡写真を図25(a)(×
(100)15μm/目盛)と図25(b)(×(10
0)15μm/目盛)に炭酸水素ナトリウムをそれぞれ
10ppmと100ppm添加した場合の結果を示す。
Next, an embodiment for promoting the modulation electric field processing will be described. In the case where the modulated electric field treatment device of the present invention is applied to a geothermal power generation facility, a desktop test was performed to determine whether the combined use with the auxiliary agent (sodium bicarbonate) could provide more effects than the treatment with the modulated electric field treatment device alone. Was. The micrograph of the interface obtained according to the above procedure is shown in FIG.
(100) 15 μm / scale) and FIG. 25B (× (10
0) 15 μm / scale) shows the results when 10 ppm and 100 ppm of sodium hydrogen carbonate were added, respectively.

【0084】図25(a)に示す界面の状態に比較して
図25(b)に示す場合には、界面よりの小粒子が少な
く、界面から粒子が反発していることが分かる。このよ
うに補助薬剤(炭酸水素ナトリウム)の併用とその添加
量を多くすることで変調電場処理装置単独での処理以上
の効果が得られることが判明した。
In the case shown in FIG. 25B as compared with the state of the interface shown in FIG. 25A, it can be seen that the number of small particles is smaller than the interface and the particles are repelled from the interface. Thus, it was found that the combined use of the auxiliary agent (sodium bicarbonate) and an increase in the amount thereof can provide more effects than the treatment using the modulated electric field treatment apparatus alone.

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

【図1】 本発明の変調電場処理法により被処理水用配
管の内壁等にスケールが付着するのを防止するメカニズ
ムを説明する図である。
FIG. 1 is a diagram illustrating a mechanism for preventing a scale from adhering to an inner wall or the like of a pipe for treated water by a modulated electric field treatment method of the present invention.

【図2】 図2(a)は本発明の変調電場処理により発
生する渦電流の原因となる誘導電場を示す図であり、図
2(b)は、その誘導電場が極大値となり、これが電子
供与帯として還元状態となることを説明する図である。
FIG. 2A is a diagram showing an induced electric field that causes an eddy current generated by the modulated electric field processing of the present invention, and FIG. 2B is a diagram showing the induced electric field having a maximum value, which is an electron. It is a figure explaining that it becomes a reduction state as a donor zone.

【図3】 本発明の机上試験用の変調電場処理装置を示
す図である。
FIG. 3 is a diagram showing a modulated electric field processing apparatus for a desk test according to the present invention.

【図4】 本発明の机上試験用の変調電場処理装置によ
る変調電場処理効果の程度を判定をするための乾燥させ
た試料の界面部における乾燥結晶体を示す図である(図
4(a)は平面図、図4(b)は側面図)。
FIG. 4 is a diagram showing a dried crystal at an interface of a dried sample for determining the degree of a modulation electric field treatment effect by the desk test modulation electric field treatment device of the present invention (FIG. 4 (a)). Is a plan view, and FIG. 4B is a side view).

【図5】 本発明の実施の形態の変調電場処理で効果の
ある界面活性剤を含む被処理水の顕微鏡検査写真であ
る。
FIG. 5 is a microscopic photograph of water to be treated containing a surfactant effective in the modulated electric field treatment according to the embodiment of the present invention.

【図6】 本発明の実施の形態の変調電場処理で効果の
ない界面活性剤を含む被処理水の顕微鏡検査写真であ
る。
FIG. 6 is a microscopic photograph of water to be treated containing a surfactant that is ineffective in the modulated electric field treatment according to the embodiment of the present invention.

【図7】 本発明の実施の形態の変調電場処理で効果が
あまりない界面活性剤を含む被処理水の顕微鏡検査写真
である。
FIG. 7 is a microscopic inspection photograph of water to be treated containing a surfactant, which is not so effective in the modulated electric field treatment according to the embodiment of the present invention.

【図8】 本発明の実施の形態の変調電場処理で効果が
あまりないスケール障害を起こしている被処理水の顕微
鏡検査写真(図8(a))であり、図8(b)は前記被
処理水の机上試験を5回行った後の顕微鏡写真を示す。
FIG. 8 is a microscopic inspection photograph (FIG. 8A) of the water to be treated having a scale failure which is not so effective in the modulated electric field treatment according to the embodiment of the present invention, and FIG. The micrograph after carrying out the desk test of the treated water 5 times is shown.

【図9】 本発明の実施の形態の変調電場処理後の被処
理水に清缶剤を添加した場合の顕微鏡写真(図9(a)
は清缶剤10ppmを含む被処理水、図9(b)は清缶
剤200ppmを含む被処理水)である。
FIG. 9 is a micrograph of a case where a cleaning agent is added to the water to be treated after the modulation electric field treatment according to the embodiment of the present invention (FIG. 9A)
Is treated water containing 10 ppm of cleaning agent, and FIG. 9B is water to be treated containing 200 ppm of cleaning agent.

【図10】 本発明の実施の形態の変調電場処理した被
処理水にスケール防止剤を添加した場合の顕微鏡写真
(図10(a)はスケール防止剤10ppmを含む被処
理水、図10(b)はスケール防止剤200ppmを含
む被処理水)である。
FIG. 10 is a micrograph of a water to be treated which has been subjected to a modulated electric field treatment according to an embodiment of the present invention, in which a scale inhibitor is added (FIG. 10 (a) is water to be treated containing 10 ppm of a scale inhibitor, FIG. 10 (b) ) Is treated water containing 200 ppm of a scale inhibitor).

【図11】 本発明の実施の形態の変調電場処理した被
処理水に重合リン酸塩系防食剤を添加した場合の顕微鏡
写真である。
FIG. 11 is a photomicrograph when a polymerized phosphate-based anticorrosive is added to water to be treated which has been subjected to a modulated electric field treatment according to an embodiment of the present invention.

【図12】 本発明の変調電場処理を行った重合リン酸
塩系防食剤を含む被処理水の界面の様子を見た顕微鏡写
真である。
FIG. 12 is a photomicrograph showing a state of an interface of water to be treated containing a polymerized phosphate-based anticorrosive which has been subjected to a modulated electric field treatment of the present invention.

【図13】 本発明の実施の形態の変調電場処理した被
処理水にスライム防止剤を添加した場合の顕微鏡写真
(図13(a)はスライム防止剤15ppmを含む被処
理水、図13(b)はスライム防止剤200ppmを含
む被処理水)である。
FIG. 13 is a photomicrograph showing the case where a slime inhibitor is added to the water to be treated which has been subjected to the modulated electric field treatment according to the embodiment of the present invention (FIG. 13 (a) is the water to be treated containing 15 ppm of the slime inhibitor; FIG. 13 (b) ) Is treated water containing 200 ppm of a slime inhibitor.

【図14】 本発明の実施の形態の変調電場処理した被
処理水に帯電防止剤と界面活性剤を添加した場合の顕微
鏡写真(図14(a)は帯電防止剤と界面活性剤10p
pmを含む被処理水、図14(b)は帯電防止剤と界面
活性剤を200ppmを含む被処理水)である。
FIG. 14 is a micrograph of an antistatic agent and a surfactant added to water to be treated which has been subjected to a modulated electric field treatment according to the embodiment of the present invention (FIG. 14 (a) shows an antistatic agent and a surfactant 10p).
14 (b) is treated water containing 200 ppm of an antistatic agent and a surfactant).

【図15】 本発明の実施の形態の変調電場処理した被
処理水にリンス剤を添加した場合の顕微鏡写真(図15
(a)はリンス剤50ppmを含む被処理水、図15
(b)はリンス剤200ppmを含む被処理水)であ
る。
FIG. 15 is a micrograph of a case where a rinsing agent is added to the water to be treated that has been subjected to the modulated electric field treatment according to the embodiment of the present invention (FIG. 15).
(A) Treated water containing 50 ppm of a rinsing agent, FIG.
(B) is treated water containing 200 ppm of a rinsing agent).

【図16】 本発明の実施の形態の変調電場処理した被
処理水に海生物付着防止剤を添加した場合の顕微鏡写真
(図16(a)は海生物付着防止剤50ppmを含む被
処理水、図16(b)は海生物付着防止剤200ppm
を含む被処理水)である。
FIG. 16 is a micrograph of a water to be treated which has been subjected to a modulated electric field treatment according to an embodiment of the present invention, in which a marine organism adhesion inhibitor is added (FIG. 16 (a) is a water to be treated containing 50 ppm of a marine organism adhesion inhibitor; FIG. 16 (b) shows a 200 ppm anti-sea organism adhesion agent.
To-be-treated water).

【図17】 発電所設備の軸受け冷却水の循環系を示す
図である。
FIG. 17 is a diagram showing a circulation system of bearing cooling water of power plant equipment.

【図18】 図18(a)には図17の発電所設備の軸
受け冷却水の循環系のサンプリングラックの冷却器の外
側にスケールとして付着した状況を示し、図18(b)
には防食剤(重合リン酸塩)を注入したまま、本発明の
変調電場処理を4ヶ月間連続して行ったため、逆にスケ
ール障害を生じた実例を示す。
FIG. 18 (a) shows a situation where it is attached as a scale outside the cooler of the sampling rack of the bearing cooling water circulation system of the power plant equipment of FIG. 17, and FIG. 18 (b)
Shows an example in which the modulation electric field treatment of the present invention was continuously performed for four months while the anticorrosive (polymerized phosphate) was being injected, and conversely, a scale hindrance occurred.

【図19】 図19(a)には本発明の変調電場処理を
する前の前記サンプリングラックの冷却器を収納してい
るケースにスケールが付着している状態を示す写真であ
り、図19(b)には防食剤(重合リン酸塩)を含む被
処理水に対して4ヶ月間連続して本発明の変調電場処理
を行った後の前記ケーシングの内壁面を示す。
FIG. 19 (a) is a photograph showing a state in which a scale is attached to a case accommodating a cooler of the sampling rack before performing the modulated electric field treatment of the present invention, and FIG. b) shows the inner wall surface of the casing after the modulated electric field treatment of the present invention is continuously performed on the water to be treated containing the anticorrosive (polymerized phosphate) for four months.

【図20】 ディーゼル発電機の開放型冷却設備の二次
冷却水の循環流路に本発明の変調電場処理装置を適用し
たフロー図を示す。
FIG. 20 shows a flow diagram in which the modulated electric field treatment device of the present invention is applied to a circulation channel of secondary cooling water of an open-type cooling facility of a diesel generator.

【図21】 本発明の実施の形態の変調電場処理した水
道水に特定の市販スライム防止剤を加え、前記手順に従
って得た界面の顕微鏡写真(図21(a))と本発明の
実施の形態の変調電場処理した水道水に特定の市販スケ
ール防止剤を加え、前記手順に従って得た界面の顕微鏡
写真(図21(b))である。
FIG. 21 shows a micrograph (FIG. 21 (a)) of an interface obtained by adding a specific commercially available slime inhibitor to tap water subjected to a modulated electric field treatment according to the embodiment of the present invention and following the above procedure, and an embodiment of the present invention. 21B is a photomicrograph (FIG. 21 (b)) of an interface obtained by adding a specific commercial scale inhibitor to tap water treated with a modulated electric field according to the above procedure.

【図22】 図20に示す開放型冷却塔の底部に残留し
ていた乳白色ポリマー状の物質を採取し、顕微鏡写真で
ある。
FIG. 22 is a micrograph of a milky white polymeric substance remaining at the bottom of the open cooling tower shown in FIG. 20;

【図23】 スケール分散剤を含む懸濁物質を除去する
前に熱交換器でのスケール付着状況を示す写真である。
FIG. 23 is a photograph showing a scale adhesion state in a heat exchanger before removing a suspended substance containing a scale dispersant.

【図24】 ストレーナを設置して懸濁物質を除去した
後に本発明の変調電場処理を行った熱交換器を示す写真
である。
FIG. 24 is a photograph showing a heat exchanger subjected to a modulated electric field treatment according to the present invention after a suspended substance is removed by installing a strainer.

【図25】 本発明の変調電場処理を促進させる補助薬
剤(炭酸水素ナトリウム)の効果を示す机上試験の結果
を示す界面の顕微鏡写真である(図25(a)と図25
(b)に炭酸水素ナトリウムをそれぞれ10ppmと1
00ppm添加した場合の結果を示す)。
FIG. 25 is a micrograph of an interface showing the results of a desk test showing the effect of an auxiliary agent (sodium bicarbonate) that promotes the modulated electric field treatment of the present invention (FIGS. 25 (a) and 25).
(B) 10 ppm and 1 ppm of sodium hydrogen carbonate
The result when 00 ppm is added is shown).

【図26】 被処理水用配管の内壁等にスケールが付着
するメカニズムを説明する図である。
FIG. 26 is a view for explaining a mechanism by which scale adheres to an inner wall or the like of a pipe for treated water.

【符号の説明】[Explanation of symbols]

1 パイプ 2 コイル 3 変換器 4 ボトル 5 ビーカ 6 ガラス板 10 冷却水タンク 11 薬品注入設
備 12 熱交換装置 13 サンプリン
グラック 14 変調電場処理装置 15 循環冷却水
配管 17 熱交換器 18 開放型冷却
塔 19 ポンプ 20 ストレーナ
DESCRIPTION OF SYMBOLS 1 Pipe 2 Coil 3 Converter 4 Bottle 5 Beaker 6 Glass plate 10 Cooling water tank 11 Chemical injection equipment 12 Heat exchange device 13 Sampling rack 14 Modulation electric field processing device 15 Circulating cooling water pipe 17 Heat exchanger 18 Open type cooling tower 19 Pump 20 strainer

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 5/00 620 C02F 5/00 620D 1/48 1/48 B (71)出願人 500045165 Erasmusgracht 29/111 1056 BC Amsterdam The Netherlands (72)発明者 深町 進平 東京都墨田区菊川2丁目5番12号 エスケ ーエイ株式会社内 (72)発明者 大谷 裕一 東京都墨田区菊川2丁目5番12号 エスケ ーエイ株式会社内 Fターム(参考) 4D061 DA01 DA08 DB05 EB09 ED12──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 5/00 620 C02F 5/00 620D 1/48 1/48 B (71) Applicant 500045165 Erasmusgracht 29/111 1056 BC Amsterdam The Netherlands (72) Inventor Shinpei Fukamachi 2-5-12 Kikugawa, Sumida-ku, Tokyo SKAA Corporation (72) Inventor Yuichi Otani 2-5-1 Kikugawa, Sumida-ku, Tokyo SKA A shares F term in the company (reference) 4D061 DA01 DA08 DB05 EB09 ED12

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 第一の流体流路または該第一の流体流路
に導入する流体用の第二の流体流路の表面にコイルを巻
きつけ、該コイルに周波数が時間的に変化する方形波の
交流電流を流し、コイルに流れる電流により誘起される
変調電場により前記第一の流体流路又は第二の流体流路
を流れる流体を処理することにより前記第一の流体流路
を構成する壁面の錆び、スケール、その他の成分の付着
防止及び/又は除去方法において、 流体の前記変調電場処理を阻害するカチオン系薬剤を除
いた後に前記変調電場処理を行うことを特徴とする流体
流路の錆び、スケール、その他の成分の付着防止及び/
又は除去方法。
A coil is wound around a surface of a first fluid flow path or a second fluid flow path for a fluid to be introduced into the first fluid flow path, and the coil has a rectangular shape whose frequency changes with time. The first fluid flow path is constituted by flowing an alternating current of a wave and processing the fluid flowing through the first fluid flow path or the second fluid flow path by a modulated electric field induced by the current flowing through the coil. A method for preventing and / or removing rust, scale, and other components on a wall, wherein the modulated electric field treatment is performed after removing a cationic drug that inhibits the modulated electric field treatment of a fluid. Prevents rust, scale and other components from adhering and / or
Or a removal method.
【請求項2】 カチオン系薬剤は、界面活性剤、高分子
系薬剤とリン酸塩系薬剤を含む防食剤、清缶剤、スケー
ル防止剤、スライム防止剤、帯電防止剤、リンス(乾燥
仕上)剤、床ワックス剤、消泡剤及び海生物付着防止剤
から成る群から選ばれる少なくとも一つから成る薬剤で
あることを特徴とする請求項1記載の流体流路の錆び、
スケール、その他の成分の付着防止及び/又は除去方
法。
2. The cationic drug includes a surfactant, an anticorrosive containing a polymer drug and a phosphate drug, a tin can, a scale inhibitor, a slime inhibitor, an antistatic agent, and a rinse (dry finish). 2. The rust of the fluid flow path according to claim 1, wherein the agent is at least one selected from the group consisting of an agent, a floor wax agent, an antifoaming agent, and a marine organism adhesion inhibitor.
A method for preventing and / or removing scale and other components.
【請求項3】 第一の流体流路または該第一の流体流路
に導入する流体用の第二の流体流路の表面にコイルを巻
きつけ、該コイルに周波数が時間的に変化する方形波の
交流電流を流し、コイルに流れる電流により誘起される
変調電場により前記第一の流体流路又は第二の流体流路
を流れる流体を処理することにより前記第一の流体流路
を構成する壁面の錆び、スケール、その他の成分の付着
防止及び/又は除去方法において、 流体の前記変調電場処理を促進するアニオン系薬剤を添
加した後に前記変調電場処理を行うことを特徴とする流
体流路の錆び、スケール、その他の成分付着防止及び/
又は除去方法。
3. A coil having a coil wound around a surface of the first fluid flow path or a second fluid flow path for a fluid to be introduced into the first fluid flow path, wherein the coil has a rectangular shape whose frequency changes with time. The first fluid flow path is constituted by flowing an alternating current of a wave and processing the fluid flowing through the first fluid flow path or the second fluid flow path by a modulated electric field induced by the current flowing through the coil. In a method for preventing and / or removing rust, scale, and other components on wall surfaces, the modulated electric field treatment is performed after adding an anionic agent that promotes the modulated electric field treatment of a fluid. Prevents rust, scale, and other components from adhering and / or
Or a removal method.
【請求項4】 第一の流体流路または該第一の流体流路
に導入する流体用の第二の流体流路の表面にコイルを巻
きつけ、該コイルに周波数が時間的に変化する方形波の
交流電流を流し、コイルに流れる電流により誘起される
変調電場により前記第一の流体流路又は第二の流体流路
を流れる流体を処理することにより前記第一の流体流路
を構成する壁面の錆び、スケール、その他の成分の付着
防止及び/又は除去方法において、 流体の前記変調電場処理を促進する炭酸ナトリウム、炭
酸水素ナトリウム又は水酸化ナトリウムを添加した後に
前記変調電場処理を行うことを特徴とする流体流路の錆
び、スケール、その他の成分の付着防止及び/又は除去
方法。
4. A coil around a surface of a first fluid flow path or a second fluid flow path for a fluid to be introduced into the first fluid flow path, wherein the coil has a rectangular shape whose frequency changes with time. The first fluid flow path is constituted by flowing an alternating current of a wave and processing the fluid flowing through the first fluid flow path or the second fluid flow path by a modulated electric field induced by the current flowing through the coil. In a method for preventing and / or removing rust, scale, and other components on a wall surface, the method further includes performing the modulated electric field treatment after adding sodium carbonate, sodium hydrogen carbonate, or sodium hydroxide, which promotes the modulated electric field treatment of a fluid. A method for preventing and / or removing rust, scale, and other components from a fluid channel.
【請求項5】 流体が流れる第一の流体流路又は該第一
の流体流路に導入する前記流体の第二の流体流路の表面
に巻きつけられ、周波数が時間的に変化する方形波の交
流電流を流して、変調電場を誘起させるコイルと、該コ
イルに前記電流を流すための制御系統を備えた電源装置
を設置した前記第一の流体流路を構成する壁面の錆び、
スケール、その他の付着防止及び/又は除去装置におい
て、 流体の前記変調電場処理を促進するアニオン系薬剤、炭
酸ナトリウム、炭酸水素ナトリウム又は水酸化ナトリウ
ムの添加手段を設けたことを特徴とする流体流路の錆
び、スケール、その他の成分の付着防止及び/又は除去
装置。
5. A square wave whose frequency changes with time, wound around a surface of a first fluid flow path through which a fluid flows or a surface of a second fluid flow path of the fluid introduced into the first fluid flow path. Rust on the wall constituting the first fluid flow path in which a coil for inducing a modulation electric field and a power supply device having a control system for flowing the current through the coil is provided,
A fluid flow path, characterized in that a scale, or another adhesion preventing and / or removing device, is provided with a means for adding an anionic drug, sodium carbonate, sodium hydrogen carbonate or sodium hydroxide, which promotes the modulated electric field treatment of the fluid. For preventing and / or removing rust, scale and other components.
【請求項6】 流体流路を構成する壁面の錆び、スケー
ル、その他の付着を防止及び/又は除去する流体の変調
電場処理の効果を試験するための被処理水の机上試験方
法において、 周波数が時間的に変化する方形波の交流電流を流し、該
電流により流体内に変調電場を誘起させるコイルを巻い
た傾斜状に配置したパイプの内部に前記流体流路内に流
す流体と同じ流体を通過させ、 該パイプ内を通過した前記変調電場処理がなされた流体
の一部をガラス板上に滴下させた後に、常温乾燥させ、 乾燥されたガラス上の乾燥体の界面部における変化を顕
微鏡で確認して、前記流体の変調電場処理の効果の程度
を判定する流体流路を構成する壁面の錆び、スケール、
その他が付着することを防止及び/又は除去する流体の
変調電場処理の効果を試験するための被処理水の机上試
験方法。
6. A desk test method for water to be treated for testing the effect of a modulated electric field treatment of a fluid for preventing and / or removing rust, scale, and other adhesion of a wall constituting a fluid flow path, An alternating current of a square wave that changes over time is passed, and the same fluid as the fluid flowing in the fluid flow path is passed inside a pipe arranged in an inclined shape wound with a coil that induces a modulated electric field in the fluid by the current. After a part of the fluid subjected to the modulated electric field treatment that has passed through the pipe is dropped on a glass plate, it is dried at room temperature, and the change at the interface of the dried body on the dried glass is confirmed with a microscope. Then, rust on the wall surface constituting the fluid flow path to determine the degree of the effect of the modulated electric field treatment of the fluid, rust, scale,
A desk test method for water to be treated for testing the effect of a modulated electric field treatment of a fluid for preventing and / or removing other substances from adhering.
【請求項7】 流体流路を構成する壁面の錆び、スケー
ル、その他が付着することを防止及び/又は除去する流
体の変調電場処理の効果を試験するための被処理水の机
上試験装置において、 周波数が時間的に変化する方形波の交流電流を流し、該
電流により流体内に変調電場を誘起させるコイルを巻
き、内部に前記流体流路内に流す流体と同じ流体を通過
させる傾斜状に配置したパイプを備えた被処理水の机上
試験装置。
7. A desk test apparatus for water to be treated for testing the effect of a modulated electric field treatment of a fluid for preventing and / or removing rust, scale, and the like on a wall constituting a fluid flow path, An alternating current of a square wave whose frequency changes with time is passed, and a coil that induces a modulated electric field in the fluid by the current is wound, and is disposed in an inclined shape through which the same fluid as the fluid flowing in the fluid flow path is passed. Test equipment with water to be treated equipped with pipes.
【請求項8】 第一の流体流路または該第一の流体流路
に導入する流体用の第二の流体流路の表面にコイルを巻
きつけ、該コイルに周波数が時間的に変化する方形波の
交流電流を流し、コイルに流れる電流により誘起される
変調電場により前記第一の流体流路又は第二の流体流路
を流れる流体を処理することにより前記第一の流体流路
を構成する壁面の錆び、スケール、その他の成分の付着
防止及び/又は除去方法において、 まず、請求項6記載の机上試験法で試験を行い、その机
上試験法による結果が良くない場合には、電力の出力を
上げること及び/又は前記変調電場処理を阻害する薬剤
を除いた後に前記変調電場処理を行うことを特徴とする
流体流路の錆び、スケール、その他の成分の付着防止及
び/又は除去方法。
8. A rectangular coil whose frequency changes with time, wherein a coil is wound around the surface of the first fluid flow path or the second fluid flow path for a fluid to be introduced into the first fluid flow path. The first fluid flow path is constituted by flowing an alternating current of a wave and processing the fluid flowing through the first fluid flow path or the second fluid flow path by a modulated electric field induced by the current flowing through the coil. In the method for preventing and / or removing rust, scale, and other components on the wall surface, first, a test is performed by the desk test method according to claim 6, and if the result of the desk test method is not good, the electric power is output. And / or removing the agent that inhibits the modulated electric field treatment, and then performing the modulated electric field treatment, thereby preventing and / or removing rust, scale, and other components from the fluid flow path.
【請求項9】 前記変調電場処理を阻害する薬剤は、界
面活性剤、高分子系薬剤とリン酸塩系薬剤を含む防食
剤、清缶剤、スケール防止剤、スライム防止剤、帯電防
止剤、リンス(乾燥仕上)剤、床ワックス剤、消泡剤、
海生物付着防止剤及び浮遊物質から成る群から選ばれる
少なくとも一つから成ることを特徴とする請求項8記載
の流体流路の錆び、スケール、その他の成分の付着防止
及び/又は除去方法。
9. The agent that inhibits the modulated electric field treatment includes a surfactant, an anticorrosive including a polymer-based agent and a phosphate-based agent, a cleaning agent, a scale inhibitor, a slime inhibitor, an antistatic agent, Rinse (dry finish) agent, floor wax agent, defoamer,
9. The method for preventing and / or removing rust, scale, and other components of a fluid flow path according to claim 8, wherein the method comprises at least one selected from the group consisting of a marine organism adhesion inhibitor and a suspended substance.
JP2000075253A 2000-03-17 2000-03-17 Method and apparatus for preventing and / or removing rust, scale and other components from fluid flow path Expired - Fee Related JP3674676B2 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006136771A (en) * 2004-11-10 2006-06-01 Taiheiyo Cement Corp Calcium-containing water treatment method and apparatus
US7730899B2 (en) 2007-03-20 2010-06-08 Qi Ning Mai Method and apparatus for reducing deposits in petroleum pipes
JP2011255345A (en) * 2010-06-11 2011-12-22 Ska Ltd Device and method for electromagnetic wave treatment of fluid to be treated
JPWO2012020825A1 (en) * 2010-08-13 2013-10-28 株式会社志賀機能水研究所 Water electromagnetic field treatment method and electromagnetic field treatment apparatus

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006136771A (en) * 2004-11-10 2006-06-01 Taiheiyo Cement Corp Calcium-containing water treatment method and apparatus
JP4538688B2 (en) * 2004-11-10 2010-09-08 太平洋セメント株式会社 Method and apparatus for treating calcium-containing water
US7730899B2 (en) 2007-03-20 2010-06-08 Qi Ning Mai Method and apparatus for reducing deposits in petroleum pipes
US7892360B2 (en) 2007-03-20 2011-02-22 Qi Ning Mai Methods for reducing deposits in petroleum pipes
US8066817B2 (en) 2007-03-20 2011-11-29 Qi Ning Mai Method and apparatus for reducing deposits in fluid conduits
US8163099B2 (en) 2007-03-20 2012-04-24 Qi Ning Mai Method and apparatus for reducing deposits in petroleum pipes
JP2011255345A (en) * 2010-06-11 2011-12-22 Ska Ltd Device and method for electromagnetic wave treatment of fluid to be treated
JPWO2012020825A1 (en) * 2010-08-13 2013-10-28 株式会社志賀機能水研究所 Water electromagnetic field treatment method and electromagnetic field treatment apparatus
JP5844259B2 (en) * 2010-08-13 2016-01-13 株式会社志賀機能水研究所 Electromagnetic field treatment method for water

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