JP3757888B2 - Operation management method for water treatment equipment - Google Patents

Operation management method for water treatment equipment Download PDF

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Publication number
JP3757888B2
JP3757888B2 JP2002088824A JP2002088824A JP3757888B2 JP 3757888 B2 JP3757888 B2 JP 3757888B2 JP 2002088824 A JP2002088824 A JP 2002088824A JP 2002088824 A JP2002088824 A JP 2002088824A JP 3757888 B2 JP3757888 B2 JP 3757888B2
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Prior art keywords
water treatment
water
management method
cooling water
operation management
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JP2002088824A
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JP2003287396A (en
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裕介 牛島
晶 飯村
正紹 天野
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Kurita Water Industries Ltd
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Kurita Water Industries Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は水処理機器の運転管理方法に係り、特に冷却水系のスケール又はスライム防止のための水処理機器の運転管理方法に関する。
【0002】
【従来の技術】
冷却水系では、微生物によりスライムが発生し易い。特に、循環冷却水系の高濃縮運転では、冷却水の水質が悪化し、細菌、黴、藻類などの微生物群に土砂、塵埃などが混ざり合って形成されるスライムが発生し易くなり、熱交換器における熱効率の低下や通水の悪化を引き起こす。また、スライム付着部において、機器や配管の局部腐食を誘発する。
【0003】
このようなスライムによる障害を防止するために、冷却水中に含まれる塩化物イオンを電解酸化により次亜塩素酸などの塩素系酸化剤に変換し、この塩素系酸化剤を冷却水中に存在させる方法も行われている。
【0004】
即ち、冷却水系の補給水として用いられる水道水や工業用水には、通常数mg−Cl/L〜10mg−Cl/L程度の塩化物イオンが含まれていることから、循環冷却水系の冷却水には、6〜8倍の高濃縮運転で、この補給水中の塩化物イオンが濃縮されている。このため、この冷却水を電解処理することにより、冷却水中の塩化物イオンからスライム防止効果のある残留塩素(遊離塩素)を発生させることができる。この残留塩素を含む電解処理水を冷却水系に戻すことにより、スライム障害を防止することができる。
【0005】
この塩素系酸化剤を発生させるための電解処理装置では、陽極と陰極との間に外部電源を用いて直流電圧を印加すると共に、両極間に冷却水を通水する。これにより、陽極の表面において冷却水中の塩化物イオンが酸化され、次亜塩素酸などの強い酸化力を有する残留塩素が生成する。生成した残留塩素は、スライムの原因となる微生物を殺菌し、あるいは増殖を抑制するので、循環冷却水系のスライム発生を効果的に防止することができる。
【0006】
また、開放循環冷却水系では、水の循環利用に伴い、補給水中の塩類が濃縮されることによりその濃度が増加し、炭酸カルシウムやシリカなどのスケール成分が熱交換器のチューブ等に付着して伝熱阻害を引き起こす。
【0007】
このスケール防止技術として、1対の異種金属の電極を用い、この電極間に電流を発生させてスケール防止効果のある金属イオンを水系に溶出させる方法がある。例えば、アルミニウムイオンは炭酸カルシウムの析出を抑制することから、ステンレスとアルミニウム、又はカーボンとアルミニウムを陰極と陽極に組み合わせて用い、循環水中にアルミニウム電極からアルミニウムイオンを溶解させて熱交換器の炭酸カルシウムスケールの付着を低減する技術が知られている。
【0008】
【発明が解決しようとする課題】
冷却水系において、スライム障害を確実に防止するために、冷却水中の残留塩素や電気伝導度を測定し、電解処理装置の通電を制御することが行われている。また、スケール障害を確実に防止するために、金属イオン溶出用電極への通電電流値が所定範囲となるように制御することが行われている。
【0009】
本発明は、このようなスライム障害、スケール障害等を防止するための水処理機器の動作が適切に行われているか検知し、必要に応じ自動的に機能回復を行わせると共にサービスマン派遣も自動的に行うことを可能とした水処理装置の運転管理方法を提供することを目的とする。
【0010】
【課題を解決するための手段】
本発明の水処理機器の運転管理方法は、冷却水系のスケール又はスライム防止のための水処理機器に、前記水処理機器の作動状態を検出する作動状態検出装置と、前記水処理機器の機能を洗浄により回復する機能回復装置を設け、該作動状態検出装置の検出結果に基づいて該機能回復装置を作動させる水処理機器の運転管理方法であって、該機能回復装置を作動させても機能が回復しなくなったときには補修要求信号を発生させることを特徴とするものである。
【0011】
かかる水処理機器の運転管理方法によると、水処理機器の作動状態が規定範囲を外れたときには例えば電極洗浄などの機能回復運転を自動的に行う。この機能回復運転を行っても、機能が十分に回復しない場合に例えばサービスマンを派遣するよう自動的に手配することができる。
【0012】
本発明では、検出装置の検出信号を通信回線によって遠隔監視装置に送信し、該遠隔監視装置から前記補修要求信号を発生させることが好ましい。このようにすれば、国内各地に設置された水処理機器を集中して管理し、サービスマンの派遣管理を統一的に実行することができる。また、異常データを集中的に管理、蓄積し、水処理機器の改良に役立てることも可能となる。
【0013】
本発明は、冷却水系の水処理機器の運転管理に適用する。この冷却水系は国内各所に多数設置されているので、本発明を適用した場合の効果が大きい。
【0014】
【発明の実施の形態】
以下に図面を参照して本発明の実施の形態を詳細に説明する。
【0015】
図1は本発明の実施の形態を示す開放循環冷却水系の系統図である。
【0016】
この開放循環冷却水系では、冷却塔1から、ポンプPを有する循環配管2により冷却水が熱交換器3に送給され、戻り水が配管4より冷却塔1に戻される。5は補給水の導入配管、6はブロー配管である。
【0017】
図1の実施の形態では、冷却塔1から熱交換器3への循環配管2に金属イオン発生装置7を設け、循環冷却水中に金属イオンを溶出させる。
【0018】
この金属イオン発生装置7は、循環冷却水が流通する電解槽に電極が設けられ、この電極間に直流電圧を印加する電流発生装置が設けられた構成のものである。
【0019】
溶出させる金属イオンとしては特にアルミニウムイオン、鉄イオン、亜鉛イオンが好ましく、これらは1種単独であっても2種以上溶出させても良い。従って、電極の材質としては、アルミニウム、鉄、亜鉛等が好適に用いられる。
【0020】
循環冷却水系に溶出させる金属イオンの溶出濃度には、特に制限はないが、対象水系に対して0.01ppb〜1ppm、特に0.1〜10ppbとなるように連続的に溶出させることが好ましい。この溶出濃度が0.01ppb未満では十分なスケール付着防止効果が得られず、1ppmを超えると金属塩の付着が起こる場合がある。
【0021】
この金属イオン発生装置7の前後に三方弁10,11が配置され、該三方弁10,11に、金属イオン発生装置7を迂回するバイパス配管12が接続されている。また、三方弁10,11と金属イオン発生装置7との間の配管から分岐配管13,14が分岐し、該分岐配管13,14が洗浄ユニット15に接続されている。この洗浄ユニット15は金属イオン発生装置7の電極を洗浄するためのものであり、洗浄液を貯蔵しておくタンクと、このタンク内の洗浄液を金属イオン発生装置7に循環供給するためのポンプとを備えている。この洗浄液としては、過酸化水素系薬剤、塩酸系薬剤、キレート系薬剤、有機系スライムコントロール剤などが用いられる。
【0022】
金属イオン発生装置7には、水と接する電極の起電力を測定するための起電力計が設けられている。金属イオン発生装置7の電極にスケールが付着すると電極の起電力が低下するようになるので、起電力が所定範囲を下回ったときには洗浄ユニット15を作動させるよう構成されている。
【0023】
定常の冷却塔稼動時には、三方弁10はポンプPと金属イオン発生装置7を連通し、三方弁11は金属イオン発生装置7と熱交換器3と連通する流路選択となっているが、洗浄時には、三方弁10,11はポンプPからの水がバイパス配管12を通って熱交換器3へ供給するように切り換わる。この状態において洗浄ユニット15が作動し、金属イオン発生装置7に洗浄ユニット15から洗浄液が循環流通される。
【0024】
冷却塔1には、冷却水の電気伝導度を検知する電気伝導度計20が設けられており、この電気伝導度計20の検出値が濃縮管理装置21に入力され、濃縮管理装置21は、電気伝導度が規定範囲内に納まるように補給水配管5のバルブ5aとブロー配管6のバルブ6aを制御する。
【0025】
また、この冷却塔1内の水は、ポンプPを有する配管31、濾過装置32、三方弁33、電解処理装置34、三方弁35を介して循環される。この濾過装置32としては、上向流式濾過装置、砂濾過装置、フィルター式濾過装置などが用いられる。電解処理装置34は、電解槽内に1対の電極を配置し、この電極に電圧を印加して水中の塩化物イオンから塩素系酸化剤を生成させるものである。
【0026】
冷却塔1には、冷却水のORP(酸化還元電位)を計測するためのORP計30が設けられており、電解処理装置34は、このORP計30の検出ORPが所定範囲内となるように電極間の印加電圧が制御される。
【0027】
上記の三方弁33,35間には、電解処理装置34を迂回するバイパス配管36が架設されている。
【0028】
また、三方弁33と電解処理装置34との間及び三方弁35と電解処理装置34との間からはそれぞれ分岐配管37,38が分岐しており、該分岐配管37,38は電解処理装置34の電極洗浄用の洗浄ユニット39に接続されている。この洗浄ユニット39は、洗浄液を貯留するためのタンクと、該タンク内の洗浄液を電解処理装置34に循環供給するためのポンプとを備えている。
【0029】
この洗浄液としては、希塩酸、希硫酸、キレート系薬剤などが用いられる。
【0030】
電解処理装置34には、電解電圧を測定するための電圧測定システムが設けられており、実際の電解電圧と理論電解電圧との比が所定範囲を上回ったときには洗浄ユニット39を作動させるよう構成されている。即ち、電解処理装置34の電極にスケールやスライムが付着すると所定電流を流すために電極間に印加する電圧が上昇するので、この印加電圧と理論印加電圧の比が所定値以上となったときに電極を洗浄する。
【0031】
定常の冷却塔稼動時には、三方弁33は濾過装置32と電解処理装置34を連通し、三方弁35は電解処理装置34と冷却塔1と連通する流路選択となっているが、洗浄時には、三方弁33,35は濾過装置32からの水がバイパス配管36を通って冷却塔1へ戻るように切り換わる。この状態において洗浄ユニット39が作動し、電解処理装置34に洗浄ユニット39から洗浄液が循環流通される。
【0032】
なお、三方弁33,35の代りに開閉弁を設け、バイパス配管36を省略し、洗浄ユニット39の作動時にはポンプPを停止し、該開閉弁を閉としてもよい。
【0033】
この冷却水系においては、金属イオン発生装置7及び電解処理装置34は自動的に洗浄が行なわれるので、長期にわたりサービスマンによるメンテナンスなしに運転が継続される。
【0034】
この間、金属イオン発生装置7、濃縮管理装置21、電解処理装置34の運転データと、電気伝導度計20及びORP計30の検出データは、それぞれ通信機器40を介して集中管理センターに送信され、集中管理センターのホストコンピュータに蓄積されている。
【0035】
上記の洗浄ユニット15,39が作動しても金属イオン発生装置7及び電解処理装置34の動作が定常状態に復帰しないようになったときには、金属イオン発生装置7及び電解処理装置34は補修要求信号を発生し、この補修要求信号が通信機器40から集中管理センターに通報される。集中管理センターは、この補修要求信号に基づいてサービスマン派遣センターにサービスマンの派遣を要求する信号を送信する。
【0036】
派遣要請を受けたサービスマンは、ホストコンピュータから当該冷却水系の運転履歴データを引き出し、交換用部品(例えば電極やセンサ、パッキン等)及び工具等を携行して現地に赴き、修理を行う。
【0037】
【発明の効果】
以上の通り、本発明によると、冷却水プラントを長期にわたりメンテナンスフリーで運転継続できると共に、サービスマンによる補修が必要となったときには迅速にサービスマンを派遣して補修を行うことができる。また、全国各地に設けられた多数の冷却水プラントを少人数のサービスマンで保守することができる。
【図面の簡単な説明】
【図1】実施の形態に係る水処理機器の運転管理方法が適用される冷却水系の系統図である。
【符号の説明】
1 冷却塔
3 熱交換器
7 金属イオン発生装置
10,11 三方弁
15 洗浄ユニット
20 電気伝導度計
21 濃縮管理装置
30 ORP計
32 濾過装置
33,35 三方弁
34 電解処理装置
39 洗浄ユニット
40 通信機器
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to the operation management method of water treatment equipment, in particular to the operation management how water treatment equipment for scale or slime preventing cooling water system.
[0002]
[Prior art]
In the cooling water system, slime is easily generated by microorganisms. In particular, in the high concentration operation of the circulating cooling water system, the quality of the cooling water deteriorates, and it becomes easy to generate slime that is formed by mixing soil, dust, etc. with microorganisms such as bacteria, cocoons and algae. Cause deterioration of heat efficiency and water flow. In addition, local corrosion of equipment and piping is induced in the slime adhesion part.
[0003]
In order to prevent such damage caused by slime, a method in which chloride ions contained in cooling water are converted into a chlorine-based oxidizing agent such as hypochlorous acid by electrolytic oxidation, and this chlorine-based oxidizing agent is present in the cooling water. Has also been done.
[0004]
That is, the tap water or industrial water used as make-up water for the cooling water system, usually several mg-Cl - / L~10mg-Cl - / L of about from that it contains chloride ions, the circulating cooling water system In the cooling water, chloride ions in the makeup water are concentrated by a 6-8 times high concentration operation. For this reason, by subjecting this cooling water to electrolytic treatment, residual chlorine (free chlorine) having a slime prevention effect can be generated from chloride ions in the cooling water. By returning the electrolytically treated water containing residual chlorine to the cooling water system, slime failure can be prevented.
[0005]
In this electrolytic treatment apparatus for generating a chlorinated oxidant, a DC voltage is applied between an anode and a cathode using an external power source, and cooling water is passed between both electrodes. As a result, chloride ions in the cooling water are oxidized on the surface of the anode, and residual chlorine having strong oxidizing power such as hypochlorous acid is generated. The generated residual chlorine sterilizes microorganisms that cause slime, or suppresses growth, so that generation of slime in the circulating cooling water system can be effectively prevented.
[0006]
In an open circulation cooling water system, the concentration of salts in the makeup water increases due to the circulation and use of water, and scale components such as calcium carbonate and silica adhere to the tubes of the heat exchanger. Causes heat transfer inhibition.
[0007]
As this scale prevention technique, there is a method in which a pair of electrodes of different metals are used and a current is generated between the electrodes to elute metal ions having a scale prevention effect into an aqueous system. For example, since aluminum ions suppress the precipitation of calcium carbonate, stainless steel and aluminum, or carbon and aluminum are used in combination with the cathode and anode, and the aluminum ions are dissolved from the aluminum electrode in the circulating water to heat the calcium carbonate in the heat exchanger. Techniques for reducing scale adhesion are known.
[0008]
[Problems to be solved by the invention]
In the cooling water system, in order to reliably prevent slime failure, residual chlorine and electric conductivity in the cooling water are measured to control energization of the electrolytic treatment apparatus. In addition, in order to reliably prevent scale failure, control is performed so that the value of the current applied to the metal ion elution electrode is within a predetermined range.
[0009]
The present invention detects whether the operation of the water treatment equipment for preventing such slime failure, scale failure, etc. is properly performed, and automatically restores the function as necessary and automatically dispatches service personnel. An object of the present invention is to provide an operation management method for a water treatment apparatus that can be performed automatically.
[0010]
[Means for Solving the Problems]
The operation management method for a water treatment device according to the present invention provides an operation state detection device for detecting an operation state of the water treatment device and a function of the water treatment device in a water treatment device for cooling water system scale or slime prevention. Provided is a function recovery device that recovers by cleaning , and is an operation management method for a water treatment device that operates the function recovery device based on a detection result of the operation state detection device, and functions even if the function recovery device is operated. A repair request signal is generated when recovery is not possible.
[0011]
According to the operation management method for water treatment equipment, when the operation state of the water treatment equipment is out of the specified range, function recovery operation such as electrode cleaning is automatically performed . Be carried out this function recovery operation, function has not sufficiently recovered if, it is possible to arrange automatically as for example to dispatch a service engineer.
[0012]
In the present invention, it is preferable that the detection signal of the detection device is transmitted to the remote monitoring device via a communication line, and the repair request signal is generated from the remote monitoring device. In this way, it is possible to centrally manage the water treatment equipment installed in various parts of the country, and perform dispatch management of service personnel in a unified manner. In addition, abnormal data can be centrally managed and stored, which can be used to improve water treatment equipment.
[0013]
The present invention, that apply to the operation management of the water treatment equipment cooling water system. Since many cooling water systems are installed in various places in the country, the effect when the present invention is applied is great.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
[0015]
FIG. 1 is a system diagram of an open circulation cooling water system showing an embodiment of the present invention.
[0016]
In this open circulation cooling water system, the cooling water is supplied from the cooling tower 1 to the heat exchanger 3 through the circulation pipe 2 having the pump P 1 , and the return water is returned to the cooling tower 1 through the pipe 4. 5 is a supply water introduction pipe, and 6 is a blow pipe.
[0017]
In the embodiment of FIG. 1, a metal ion generator 7 is provided in the circulation pipe 2 from the cooling tower 1 to the heat exchanger 3 to elute metal ions into the circulating cooling water.
[0018]
The metal ion generator 7 has a configuration in which electrodes are provided in an electrolytic cell through which circulating cooling water flows, and a current generator that applies a DC voltage is provided between the electrodes.
[0019]
As the metal ions to be eluted, aluminum ions, iron ions and zinc ions are particularly preferable, and these may be used alone or in combination of two or more. Accordingly, aluminum, iron, zinc or the like is preferably used as the electrode material.
[0020]
The elution concentration of metal ions to be eluted in the circulating cooling water system is not particularly limited, but it is preferable to elute continuously so as to be 0.01 ppb to 1 ppm, particularly 0.1 to 10 ppb with respect to the target water system. If this elution concentration is less than 0.01 ppb, sufficient scale adhesion preventing effect cannot be obtained, and if it exceeds 1 ppm, adhesion of metal salt may occur.
[0021]
Three-way valves 10 and 11 are arranged before and after the metal ion generator 7, and a bypass pipe 12 that bypasses the metal ion generator 7 is connected to the three-way valves 10 and 11. Further, branch pipes 13 and 14 branch from the pipe between the three-way valves 10 and 11 and the metal ion generator 7, and the branch pipes 13 and 14 are connected to the cleaning unit 15. The cleaning unit 15 is for cleaning the electrodes of the metal ion generator 7, and has a tank for storing the cleaning liquid and a pump for circulating and supplying the cleaning liquid in the tank to the metal ion generator 7. I have. As this cleaning solution, a hydrogen peroxide chemical, a hydrochloric acid chemical, a chelate chemical, an organic slime control agent, or the like is used.
[0022]
The metal ion generator 7 is provided with an electromotive force meter for measuring an electromotive force of an electrode in contact with water. When the scale adheres to the electrode of the metal ion generator 7, the electromotive force of the electrode decreases, so that the cleaning unit 15 is operated when the electromotive force falls below a predetermined range.
[0023]
The steady state of the cooling tower operation, the three-way valve 10 communicates with a pump P 1 and the metal ion generator 7, although the three-way valve 11 has a flow path selection for communication with the metal ion generating device 7 and the heat exchanger 3, At the time of cleaning, the three-way valves 10 and 11 are switched so that the water from the pump P 1 is supplied to the heat exchanger 3 through the bypass pipe 12. In this state, the cleaning unit 15 operates, and the cleaning liquid is circulated from the cleaning unit 15 to the metal ion generator 7.
[0024]
The cooling tower 1 is provided with an electrical conductivity meter 20 for detecting the electrical conductivity of the cooling water, and the detected value of the electrical conductivity meter 20 is input to the concentration management device 21, The valve 5a of the makeup water pipe 5 and the valve 6a of the blow pipe 6 are controlled so that the electric conductivity falls within the specified range.
[0025]
The water in the cooling tower 1, a pipe 31 having a pump P 2, filtration unit 32, the three-way valve 33, the electrolytic processing apparatus 34, is circulated through the three-way valve 35. As the filtration device 32, an upward flow filtration device, a sand filtration device, a filter filtration device, or the like is used. The electrolytic treatment apparatus 34 has a pair of electrodes arranged in an electrolytic cell, and applies a voltage to the electrodes to generate a chlorine-based oxidant from chloride ions in water.
[0026]
The cooling tower 1 is provided with an ORP meter 30 for measuring the ORP (oxidation-reduction potential) of the cooling water, and the electrolytic treatment apparatus 34 is configured so that the detected ORP of the ORP meter 30 falls within a predetermined range. The applied voltage between the electrodes is controlled.
[0027]
A bypass pipe 36 that bypasses the electrolytic treatment device 34 is installed between the three-way valves 33 and 35.
[0028]
Further, branch pipes 37 and 38 branch from between the three-way valve 33 and the electrolytic treatment apparatus 34 and between the three-way valve 35 and the electrolytic treatment apparatus 34, respectively. Are connected to a cleaning unit 39 for electrode cleaning. The cleaning unit 39 includes a tank for storing the cleaning liquid and a pump for circulatingly supplying the cleaning liquid in the tank to the electrolytic treatment apparatus 34.
[0029]
As this cleaning solution, dilute hydrochloric acid, dilute sulfuric acid, chelating chemicals and the like are used.
[0030]
The electrolytic treatment apparatus 34 is provided with a voltage measurement system for measuring the electrolytic voltage, and is configured to operate the cleaning unit 39 when the ratio of the actual electrolytic voltage and the theoretical electrolytic voltage exceeds a predetermined range. ing. That is, when scale or slime adheres to the electrodes of the electrolytic processing apparatus 34, the voltage applied between the electrodes rises in order to flow a predetermined current, and therefore when the ratio of the applied voltage and the theoretical applied voltage becomes a predetermined value or more. Clean the electrode.
[0031]
During normal cooling tower operation, the three-way valve 33 communicates with the filtration device 32 and the electrolytic treatment device 34, and the three-way valve 35 is selected as a flow path that communicates with the electrolytic treatment device 34 and the cooling tower 1. The three-way valves 33 and 35 are switched so that the water from the filtration device 32 returns to the cooling tower 1 through the bypass pipe 36. In this state, the cleaning unit 39 operates, and the cleaning liquid is circulated from the cleaning unit 39 to the electrolytic treatment apparatus 34.
[0032]
Incidentally, the opening and closing valve provided in place of the three-way valve 33, 35, omitting the bypass pipe 36, a pump P 2 is stopped during operation of the cleaning unit 39, the on-off valve may be closed.
[0033]
In this cooling water system, since the metal ion generator 7 and the electrolytic treatment apparatus 34 are automatically cleaned, the operation is continued for a long time without maintenance by a service person.
[0034]
During this time, the operation data of the metal ion generator 7, the concentration management device 21, the electrolytic treatment device 34, and the detection data of the electrical conductivity meter 20 and the ORP meter 30 are transmitted to the centralized management center via the communication device 40, respectively. It is stored on the host computer in the central management center.
[0035]
When the operations of the metal ion generator 7 and the electrolytic treatment apparatus 34 do not return to the steady state even when the cleaning units 15 and 39 are operated, the metal ion generator 7 and the electrolytic treatment apparatus 34 send a repair request signal. This repair request signal is reported from the communication device 40 to the central control center. The central management center transmits a signal requesting the dispatch of the service person to the service person dispatch center based on the repair request signal.
[0036]
Upon receiving the dispatch request, the service person pulls out the operation history data of the cooling water system from the host computer, carries replacement parts (for example, electrodes, sensors, packing, etc.), tools, etc., and visits the site for repair.
[0037]
【The invention's effect】
As described above, according to the present invention, the cooling water plant can be operated without maintenance for a long time, and when a repair by a service person is necessary, the service person can be dispatched and repaired quickly. In addition, a large number of cooling water plants installed throughout the country can be maintained by a small number of service personnel.
[Brief description of the drawings]
FIG. 1 is a system diagram of a cooling water system to which an operation management method for water treatment equipment according to an embodiment is applied.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Cooling tower 3 Heat exchanger 7 Metal ion generator 10,11 Three-way valve 15 Cleaning unit 20 Conductivity meter 21 Concentration management device 30 ORP meter 32 Filtration device 33,35 Three-way valve 34 Electrolytic processing device 39 Cleaning unit 40 Communication equipment

Claims (3)

冷却水系のスケール又はスライム防止のための水処理機器に、前記水処理機器の作動状態を検出する作動状態検出装置と、前記水処理機器の機能を洗浄により回復する機能回復装置を設け、該作動状態検出装置の検出結果に基づいて該機能回復装置を作動させる水処理機器の運転管理方法であって、
該機能回復装置を作動させても機能が回復しなくなったときには補修要求信号を発生させることを特徴とする水処理機器の運転管理方法。
An operation state detection device for detecting an operation state of the water treatment device and a function recovery device for recovering the function of the water treatment device by washing are provided in a water treatment device for preventing a scale or slime of a cooling water system, An operation management method for water treatment equipment for operating the function recovery device based on the detection result of the state detection device,
An operation management method for a water treatment apparatus, wherein a repair request signal is generated when the function is not recovered even when the function recovery device is operated.
請求項1において、前記検出装置の検出信号を通信回線によって遠隔監視装置に送信し、該遠隔監視装置から前記補修要求信号を発生させることを特徴とする水処理機器の運転管理方法。  2. The operation management method for water treatment equipment according to claim 1, wherein a detection signal of the detection device is transmitted to a remote monitoring device via a communication line, and the repair request signal is generated from the remote monitoring device. 請求項1又は2において、前記水処理機器は、水を電解処理するか又は金属イオンを溶出させるための電極を備えており、前記機能回復装置は、該電極を洗浄する洗浄装置であることを特徴とする水処理機器の運転管理方法。  3. The water treatment apparatus according to claim 1, wherein the water treatment device includes an electrode for electrolytically treating water or eluting metal ions, and the function recovery device is a washing device for washing the electrode. An operation management method for water treatment equipment.
JP2002088824A 2002-03-27 2002-03-27 Operation management method for water treatment equipment Expired - Fee Related JP3757888B2 (en)

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