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JP4604664B2 - Chlorine generator - Google Patents
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JP4604664B2 - Chlorine generator - Google Patents

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Publication number
JP4604664B2
JP4604664B2 JP2004323299A JP2004323299A JP4604664B2 JP 4604664 B2 JP4604664 B2 JP 4604664B2 JP 2004323299 A JP2004323299 A JP 2004323299A JP 2004323299 A JP2004323299 A JP 2004323299A JP 4604664 B2 JP4604664 B2 JP 4604664B2
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time
water
tank
residual chlorine
electrolytic cell
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JP2006130430A (en
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弘行 垣内
健二 武藤
直之 津崎
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Fuji Electric Retail Systems Co Ltd
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Fuji Electric Retail Systems Co Ltd
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Description

この発明は、ビルやマンションなどの貯水槽に貯留される水道水の残留塩素濃度を維持
するための塩素発生装置に関する。
The present invention relates to a chlorine generator for maintaining the residual chlorine concentration of tap water stored in a water storage tank such as a building or a condominium.

一般にビルやマンションなどでは、地上の受水槽で受水した水道水を屋上の貯水槽(高
置水槽)にポンプアップし、この貯水槽から各蛇口に水を供給するようにしている。とこ
ろが、高置水槽は開放型のタンクであり、水道水の滞留時間が長くなると塩素が抜け、雑
菌が繁殖しやすくなる。一方、水道法では、水道の蛇口での残留塩素濃度は0.1mg/l
以上と定められているが、安全な水質を維持するためには0.3〜0.5mg/lの残留塩素濃
度が必要であるとされている。そこで、水道水に含まれる塩素イオンを利用して塩素を発
生させ、貯水槽内の水の残留塩素濃度の維持を図る塩素発生装置が開発され、このような
装置については、例えば特許文献1に記載されている。
In general, in buildings and condominiums, tap water received in a water receiving tank on the ground is pumped up to a water storage tank (elevated water tank), and water is supplied from the water storage tank to each faucet. However, the elevated water tank is an open-type tank, and when the residence time of tap water becomes longer, chlorine is released and germs are easily propagated. On the other hand, in the Waterworks Law, the residual chlorine concentration at the tap is 0.1 mg / l.
Although it is defined as above, it is said that a residual chlorine concentration of 0.3 to 0.5 mg / l is necessary to maintain safe water quality. Therefore, a chlorine generator that generates chlorine using chlorine ions contained in tap water and maintains the residual chlorine concentration of the water in the water tank has been developed. Are listed.

図4は、このような水質度維持装置を有する貯水槽の一般構成を示す概略図である。図
4において、1はビルの屋上などに設置される貯水槽で、地上に設置された図示しない受
水槽からポンプアップされた水道水が貯留されている。貯水槽1内の水道水は給水口2か
ら各階の蛇口に給水され、水位が下がると図示しない水位センサからの検知信号により補
給口3から補給される。この貯水槽1内の水道水は塩素で殺菌されているが、すでに述べ
たように滞留時間の経過とともに次第に塩素が抜けて雑菌が繁殖しやすくなる。そのため
、貯水槽1と並んで残留塩素濃度の維持を図る塩素発生装置4が設置されている。貯水槽
1の水道水は塩素発生装置4を通して循環することにより、残留塩素濃度の維持が図られ
ている。
FIG. 4 is a schematic view showing a general configuration of a water storage tank having such a water quality maintaining device. In FIG. 4, reference numeral 1 denotes a water storage tank installed on the rooftop of a building, in which tap water pumped up from a water receiving tank (not shown) installed on the ground is stored. The tap water in the water tank 1 is supplied from the water supply port 2 to the faucet on each floor, and when the water level drops, it is supplied from the supply port 3 by a detection signal from a water level sensor (not shown). Although the tap water in the water tank 1 is sterilized with chlorine, as described above, the chlorine gradually disappears as the residence time elapses, so that germs can easily propagate. Therefore, a chlorine generator 4 is installed along with the water tank 1 to maintain the residual chlorine concentration. The tap water in the water tank 1 is circulated through the chlorine generator 4 to maintain the residual chlorine concentration.

塩素発生装置4は、水道水を電気分解して塩素イオンから次亜塩素酸を発生させる電解
槽5と、貯水槽1内の水道水を電解槽5を通して循環させる循環ポンプ6とを備えている
。周知の通り、電解槽5は密閉された容器内に正負2枚の平板な電極7を有し、電極7は
微小な隙間を介して対向配置されている。電解槽5及び循環ポンプ6は、例えば1日の運
転回数、運転時刻、1回当りの運転時間などが予め定められており、制御部8は運転時刻
になると所定の時間、電解槽5の電極間に所定の直流電流を通流しながら循環ポンプ6を
運転する。これにより、貯水槽1内の水道水は電極間を通過しながら電気分解を受け、塩
素イオンが次亜塩素酸に変換されて、貯水槽1内の水の残留塩素濃度が一定範囲に維持さ
れる。
特開2000−153885号公報
The chlorine generator 4 includes an electrolytic tank 5 that electrolyzes tap water to generate hypochlorous acid from chlorine ions, and a circulation pump 6 that circulates the tap water in the water storage tank 1 through the electrolytic tank 5. . As is well known, the electrolytic cell 5 has two plates of positive and negative flat electrodes 7 in a sealed container, and the electrodes 7 are arranged to face each other through a minute gap. For example, the number of operations per day, the operation time, and the operation time per operation of the electrolytic cell 5 and the circulation pump 6 are determined in advance, and the control unit 8 sets the electrodes of the electrolytic cell 5 for a predetermined time when the operation time is reached. The circulating pump 6 is operated while a predetermined direct current is passed between them. Thereby, the tap water in the water tank 1 is electrolyzed while passing between the electrodes, the chlorine ions are converted into hypochlorous acid, and the residual chlorine concentration of the water in the water tank 1 is maintained within a certain range. The
Japanese Patent Laid-Open No. 2000-153858

ところで、水道水を貯留する貯水槽は、内部の劣化を防止するために、定期的な点検・
清掃に合わせて再塗装などの補修作業を行うことがある。これらの作業は貯水槽からの水
の供給を停止して実施され、極力短時間で終了するように行われる。そのため、作業時間
が十分に取れず、貯水槽も再塗装による塗料が完全に硬化する前に給水を開始する場合が
ある。この場合、塗料は水中で硬化が徐々に進行するが、その間は塗料中の有機物質との
反応により水中の残留塩素濃度は平常時に比べ大幅に低下する。このような現象は、新規
の給水装置の運転立ち上げや船舶が出航する前の貯水槽整備等の場合における塗料や油分
などの影響によっても生じる。
By the way, water tanks that store tap water are regularly checked and
Repair work such as repainting may be performed in accordance with cleaning. These operations are performed with the supply of water from the water tank stopped, and are performed in a short time as much as possible. For this reason, there is a case where the working time cannot be taken sufficiently and the water tank starts to supply water before the paint by repainting is completely cured. In this case, the coating gradually cures in water, but during that time, the residual chlorine concentration in the water is significantly reduced compared to the normal time due to the reaction with the organic substance in the coating. Such a phenomenon also occurs due to the influence of paint, oil, and the like in the case of starting up a new water supply device or maintaining a water tank before the ship leaves.

そこで、この発明の課題は、空の貯水槽に初めて水道水を充填した際の残留塩素濃度の
大幅な低下を防止することにある。
Accordingly, an object of the present invention is to prevent a significant decrease in residual chlorine concentration when tap water is first filled in an empty water tank.

上記課題を解決するために、この発明は貯水槽に貯留された水道水を電気分解して残留塩素を発生させる電解槽を備え、予め設定された時刻又は時間間隔で所定時間、前記貯留水を、前記電解槽を通して循環させるとともに前記電解槽に通電し、前記貯留水の残留塩素濃度を一定範囲に維持する塩素発生装置において、
空の前記貯水槽に水道水を充填した後、一定時間を経過するまでの初期期間は、その後の定常状態よりも前記電解槽の通電時間を長く設定し、前記初期期間中の通電時間を経過時間とともに前記定常状態の通電時間まで次第に減少させるようにしたことを特徴とする(請求項1)。
In order to solve the above problems, the present invention includes an electrolytic cell that electrolyzes tap water stored in a water storage tank to generate residual chlorine, and the stored water is stored for a predetermined time at a preset time or time interval. In the chlorine generator that circulates through the electrolytic cell and energizes the electrolytic cell to maintain the residual chlorine concentration in the stored water in a certain range,
After filling the empty water tank with tap water, the initial period until a certain time elapses is set so that the energization time of the electrolyzer is longer than the subsequent steady state , and the energization time during the initial period elapses. The power consumption is gradually decreased with time until the energization time in the steady state (claim 1).

請求項1の発明によれば、初期給水後、一定時間は電解槽の通電時間を定常状態よりも延長することにより、この間の残留塩素発生量を増加させ、塗料等の影響による残留塩素の消費を補うことができる。   According to the first aspect of the present invention, after the initial water supply, the energization time of the electrolytic cell is extended for a certain period of time from the steady state, thereby increasing the amount of residual chlorine generated during this period, and the consumption of residual chlorine due to the influence of paint, etc. Can be supplemented.

そして、塗料等の影響は時間とともに低減する。従って、通電時間の延長も経過時間とともに抑えるのがよく、これにより残留塩素の過剰な生成による塩素臭の発生を防止することができる。   And the influence of a paint etc. reduces with time. Therefore, the extension of the energization time is preferably suppressed with the elapsed time, and thereby generation of chlorine odor due to excessive generation of residual chlorine can be prevented.

請求項の発明において、経過時間とともに減少させる前記通電時間のパターンを前記初期期間中に所定の周期で繰り返すようにすることができる(請求項2)。 In the first aspect of the present invention, the energization time pattern that decreases with the elapsed time can be repeated at a predetermined period during the initial period (second aspect).

この発明によれば、空の貯水槽に水道水を充填した後の初期期間において、残留塩素発生量を定常状態よりも増加させることにより、塗料等の影響により残留塩素が過剰に消費されることによる残留塩素濃度の低下を補い、常に適正な水質を維持することができる。   According to this invention, in the initial period after filling an empty water tank with tap water, residual chlorine is excessively consumed due to the influence of paint, etc. by increasing the amount of residual chlorine generated from the steady state. It can compensate for the decrease in residual chlorine concentration due to water and can always maintain an appropriate water quality.

以下、図1〜図3に基づいて、この発明の実施の形態を説明する。   Embodiments of the present invention will be described below with reference to FIGS.

図1は、この発明の実施例1を示す線図で、横軸は空の貯水槽に水道水を充填した後の経過時間(h)、縦軸は電解槽の通電時間(min)である。この実施例1は、例えば貯水槽を再塗装した場合に、水道水を充填した後の最初の10時間は、塗料等との反応により貯留水中の残留塩素濃度の低下が大きくなる場合を想定し、その間は定常状態よりも電解槽の通電時間を長くする例を示している。すなわち、図1において、定常状態(10時間経過後)の通電時間は30分とし、初期期間では最初は60分とし、その後、徐々に減少させて10時間経過後に30分としている。   FIG. 1 is a diagram showing Example 1 of the present invention, in which the horizontal axis is the elapsed time (h) after filling an empty water tank with tap water, and the vertical axis is the energization time (min) of the electrolytic cell. . In Example 1, for example, when the water tank is repainted, the first 10 hours after filling with tap water assumes a case where the decrease in residual chlorine concentration in the stored water becomes large due to the reaction with the paint or the like. In the meantime, an example in which the energization time of the electrolytic cell is made longer than in the steady state is shown. That is, in FIG. 1, the energization time in the steady state (after 10 hours) is 30 minutes, initially 60 minutes, and then gradually decreased to 30 minutes after 10 hours.

塩素発生装置は、例えば毎時(1時間ごと)に自動運転され、各回の通電時間は水道水充填後の経過時間に応じて、図示線図に基づいて可変される。このような通電時間の可変制御によれば、空の貯水槽に水道水を充填した当初の残留塩素濃度の著しい低下を補うことができ、また時間経過に伴う塗料等の影響の低下に応じて通電時間を徐々に減少させることにより、残留塩素の過度の発生を抑えて塩素臭を防止することができる。   The chlorine generator is automatically operated, for example, every hour (every hour), and each energization time is varied based on the diagram in accordance with the elapsed time after filling with tap water. According to such variable control of the energization time, it is possible to compensate for a significant decrease in the initial residual chlorine concentration when tap water is filled in an empty water tank, and in accordance with a decrease in the influence of paint, etc. over time. By gradually reducing the energization time, excessive generation of residual chlorine can be suppressed and chlorine odor can be prevented.

図2は、この発明の実施例2を示す線図で、横軸は空の貯水槽に水道水を充填した後の経過時間(h)、縦軸は電解槽の通電時間(min)である。この実施例2は、水道水を充填した後の最初の30時間は、塗料等との反応により貯留水中の残留塩素濃度の低下が大きくなる場合を想定し、その間は定常状態よりも電解槽の通電時間を長くし、かつ通電時間を時間の経過に応じて徐々に減少させるとともに、この減少パターンを複数回(図示の場合は3回)繰り返す例を示している。すなわち、図2において、定常状態(30時間経過後)の通電時間は30分であるが、初期状態では最初を60分とし、その後、徐々に減少させて10時間経過後に30分とするとともに、この減少パターンを定常状態に至る30時間に3回繰り返している。   FIG. 2 is a diagram showing Example 2 of the present invention, in which the horizontal axis represents the elapsed time (h) after filling an empty water tank with tap water, and the vertical axis represents the energization time (min) of the electrolytic cell. . In Example 2, the first 30 hours after filling with tap water is assumed to be a case where the decrease in residual chlorine concentration in the stored water becomes large due to the reaction with the paint, etc. In the example, the energization time is lengthened and the energization time is gradually decreased as time elapses, and this reduction pattern is repeated a plurality of times (in the illustrated case, three times). That is, in FIG. 2, the energization time in the steady state (after 30 hours) is 30 minutes, but in the initial state, the first is 60 minutes, and then gradually decreases to 30 minutes after 10 hours. This decreasing pattern is repeated three times in 30 hours until the steady state is reached.

図3は、実施例2の初期運転中における経過時間(横軸)と貯水槽内の残留塩素濃度(横軸)との関係を例示した線図である。なお、図中の破線は塩素発生装置の運転がない場合、一点鎖線は通電時間を常に一定にして塩素発生装置を運転した場合、実線は図2のパターンで通電時間を変化させた場合をそれぞれ示し、かつ塩素発生装置は毎時に自動運転されるものとしている。一般に、貯水槽への水道水の補給は、水位検知信号により水位が1/3程度低下したら行われるが、図3の例では貯水槽に最初に水道水を満タンまで充填した後、12時間経過後に1回目の補給が行われ、21時間経過後に2回目の補給が行われた場合を示している。   FIG. 3 is a diagram illustrating the relationship between the elapsed time (horizontal axis) during the initial operation of Example 2 and the residual chlorine concentration in the water tank (horizontal axis). The broken line in the figure indicates that the chlorine generator is not operated, the alternate long and short dash line indicates that the energization time is always kept constant, and the solid line indicates the case where the energization time is changed in the pattern of FIG. It is assumed that the chlorine generator is automatically operated every hour. In general, replenishment of tap water to a water tank is performed when the water level is lowered by about 1/3 by a water level detection signal, but in the example of FIG. 3, the water tank is initially filled with tap water to a full tank for 12 hours. The case where the first replenishment is performed after the elapse of time and the second replenishment is performed after the elapse of 21 hours is shown.

さて、図3において、電解槽の通電がない場合、破線で示す残留塩素濃度は時間の経過とともに低下するが、特に貯水槽に初めて水道水が充填された後の図示の初期期間中には低下が著しい。低下した残留塩素濃度は、水位が低下して新たな水道水が再び満タンまで補給されると図示の通り回復する。次に、図3において、1時間ごとに一定時間、電解槽に通電した場合には、一点鎖線で示すように残留塩素濃度の回復が行われるが、初期期間中は塗料等による残留塩素の消費が大きいため充分に回復せず、残留塩素濃度は時間とともに低下する。   Now, in FIG. 3, when the electrolytic cell is not energized, the residual chlorine concentration indicated by the broken line decreases with the passage of time, but particularly during the initial period shown in the figure after the water tank is first filled with tap water. Is remarkable. The lowered residual chlorine concentration recovers as shown when the water level drops and new tap water is replenished to full tank. Next, in FIG. 3, when the electrolytic cell is energized every hour for a certain period of time, the residual chlorine concentration is recovered as indicated by the alternate long and short dash line. Is not sufficiently recovered, and the residual chlorine concentration decreases with time.

これに対して、1時間ごとに図2に定められた時間、電解槽に通電した場合には、実線で示すように、残留塩素濃度は時間の経過に関わらずほぼ一定に保たれる。これは、初期期間中は図2に基づいて通電時間を長くすることにより、塗料等の影響により残留塩素の多大な消費を補うことによる。このように、空の貯水槽に初めて水道水を充填した後の初期運転中は、電解槽の通電時間を定常状態よりも長くすることにより、塗料や油分による残留塩素濃度の過度の低下を防止することができ、また時間経過とともに通電時間を徐々に減少させることにより、必要以上の残留塩素の発生を抑えて塩素臭を防止することができる。   On the other hand, when the electrolytic cell is energized for the time set in FIG. 2 every hour, as shown by the solid line, the residual chlorine concentration is kept almost constant regardless of the passage of time. This is because, during the initial period, the energization time is lengthened based on FIG. 2 to compensate for the great consumption of residual chlorine due to the influence of the paint and the like. In this way, during the initial operation after filling tap water into the empty water tank for the first time, the energization time of the electrolytic cell is made longer than the steady state, thereby preventing an excessive decrease in the residual chlorine concentration due to paint and oil. Further, by gradually reducing the energization time with the passage of time, generation of excessive residual chlorine can be suppressed and a chlorine odor can be prevented.

この発明の実施例1を示す線図である。It is a diagram which shows Example 1 of this invention. この発明の実施例2を示す線図である。It is a diagram which shows Example 2 of this invention. 実施例2における残留塩素濃度の経時変化を示す線図である。FIG. 6 is a diagram showing a change with time in residual chlorine concentration in Example 2. 塩素発生装置の一般的な構成を示すシステム図である。It is a system diagram which shows the general structure of a chlorine generator.

1 貯水槽
5 電解槽
6 循環ポンプ
7 電極
DESCRIPTION OF SYMBOLS 1 Water storage tank 5 Electrolysis tank 6 Circulation pump 7 Electrode

Claims (2)

貯水槽に貯留された水道水を電気分解して残留塩素を発生させる電解槽を備え、予め設定された時刻又は時間間隔で所定時間、前記貯留水を、前記電解槽を通して循環させるとともに前記電解槽に通電し、前記貯留水の残留塩素濃度を一定範囲に維持する塩素発生装置において、
空の前記貯水槽に水道水を充填した後、一定時間を経過するまでの初期期間は、その後の定常状態よりも前記電解槽の通電時間を長く設定し、前記初期期間中の通電時間を経過時間とともに前記定常状態の通電時間まで次第に減少させるようにしたことを特徴とする塩素発生装置。
An electrolytic cell that electrolyzes tap water stored in a water storage tank to generate residual chlorine is provided, and the stored water is circulated through the electrolytic cell for a predetermined time at a preset time or time interval, and the electrolytic cell In the chlorine generator for energizing the tank and maintaining the residual chlorine concentration of the stored water in a certain range,
After filling the empty water tank with tap water, the initial period until a certain time elapses is set so that the energization time of the electrolyzer is longer than the subsequent steady state , and the energization time during the initial period elapses. A chlorine generator characterized by gradually decreasing with time to the energization time in the steady state .
経過時間とともに減少させる前記通電時間のパターンを前記初期期間中に所定の周期で繰り返すようにしたことを特徴とする請求項記載の塩素発生装置。 Elapsed chlorine generator of the pattern of the energization time to decrease with time according to claim 1, wherein it has to repeat at a predetermined cycle during the initial period.
JP2004323299A 2004-11-08 2004-11-08 Chlorine generator Expired - Fee Related JP4604664B2 (en)

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