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JP4267755B2 - Water treatment equipment - Google Patents

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Publication number
JP4267755B2
JP4267755B2 JP14322799A JP14322799A JP4267755B2 JP 4267755 B2 JP4267755 B2 JP 4267755B2 JP 14322799 A JP14322799 A JP 14322799A JP 14322799 A JP14322799 A JP 14322799A JP 4267755 B2 JP4267755 B2 JP 4267755B2
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JP
Japan
Prior art keywords
water
silver
flow rate
supply
silver ions
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.)
Expired - Fee Related
Application number
JP14322799A
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Japanese (ja)
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JP2000325953A (en
Inventor
口 義 夫 山
野 清 司 天
村 恵 理 子 仲
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.)
Janome Corp
Original Assignee
Janome Sewing Machine Co 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
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Priority to JP14322799A priority Critical patent/JP4267755B2/en
Publication of JP2000325953A publication Critical patent/JP2000325953A/en
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Description

【0001】
【発明の属する技術分野】
この発明は、整水器や浄水器等の水処理装置に関する。
【0002】
【従来の技術】
整水器及び浄水器には、濾材として、水道水中の残留塩素、有機物等を処理するために活性炭等が用いられている。濾材を通過した後の水はこの活性炭等により消毒剤である残留塩素が取り除かれているため、長時間整水器及び浄水器を使用しない場合濾材内部の滞留水や器内に残っている残留水中の細菌が増殖する問題がある。一般的に、この細菌の増殖を抑制するために濾材内の活性炭として銀を付着させた抗菌活性炭を使用する方法が用いられている。この抗菌活性炭は水に触れると銀イオンを溶出し、この銀イオンにより、細菌の増殖を抑制することが可能である。
【0003】
【発明が解決しようとする課題】
しかし、銀を添着させた抗菌活性炭ではその銀イオンの溶出期間は数日程度であり、長期間濾材内部の滞留水や本体内に残っている残留水中の細菌増殖を抑制することができない問題がある。
本発明は上記従来技術の問題を解決することを目的とする。
【0004】
【課題を解決するための手段】
上記目的を達成するために、本発明は、濾材を備えた水処理装置において、
濾材の上流側に備えられた銀の電解により銀イオンを供給する手段と、水処理装置に供給される供給水の流量を検出する流量検出手段と、前記流量検出手段からの供給水の流量に基づいて、前記銀の電解のための電流を制御することにより、銀の電解量を制御する制御手段とを備え、該制御手段は前記銀イオンを供給する手段による銀イオンの供給を間欠的に供給するように制御する水処理装置とすることで、課題を解決した。
該銀イオンにより、水処理装置内の残留水や濾材の滞留水中の細菌の増殖を抑制することが可能になる。しかも供給水の流量を検出し、これに基づいて 銀イオンの供出量を制御することができるから、常に適正な抗菌作用を得ることができる。
該銀イオンを供給する手段からの銀イオンの供給により、下流側の濾材に吸着され、濾材から少しずつ水の中に溶け出すため、連続的な効果が得られる。
【0005】
【発明の実施の形態】
以下本発明の実施の形態を図面に基づいて説明する。
【0006】
図1に一の実施形態を示す。
図1において、浄水カートリッジ10には上流から水道水などの供給水が供給され、浄水カートリッジ10に収納された活性炭等の濾材により該供給水を浄水して下流に流すように構成されている。
該浄水カートリッジ10の上流側に銀イオン供給装置1が設けられており、供給水に連続的又は間欠的に銀イオンを添加するようになっている。供給水に添加された銀イオンは浄水カートリッジ10の濾材(活性炭など)に吸着され、銀イオン供給装置1からの銀イオンの供給が停止した後でも所定時間は抗菌作用を維持するようになっている。
【0007】
銀イオン供給装置1は銀の電解による供給装置となっており、銀溶解槽8に陽極としての銀電極6と陰極としての不溶解電極7が設けられた構造になっている。該電極6、7に所定時間毎に通電することにより銀イオンを供給水中に供給するように構成されている。不溶解電極7としては、白金、金、炭素棒、SUS、Ti、Ti−Ptを用いることが可能である
【0008】
銀イオンの溶出量は下式に示すファラデーの法則により決まる。したがって銀イオン添加による供給水の銀イオン濃度は、供給水の流量を検出し、該検出値に応じて銀電極と不溶解電極の間に流す電流値を制御すれば一定の濃度にすることができる。また任意の濃度を電流値制御により得ることができる。
銀の溶出量(g)=銀の1グラム当量(g)×{電流値(A)×時間(sec)÷96500(q)}
供給水中の銀の濃度(g/L)=銀の1グラム当量(g)×
{電流値(A)÷(96500(q)×流量(L/sec))}
【0009】
上記流量を検出するために供給水の流路中には流量カウンタ5が設けられている。この実施形態では銀イオン供給装置1と浄水カートリッジ10の間に流量カウンタ5が設けられ、供給制御装置3に流量信号を送るようになっている。
供給制御装置3は流量カウンタ5からの流量信号に基づいて上記式に従って電流値を求め、電流値制御装置30を介して銀電極6と不溶解電極7に供給する電流値を制御するようになっている。この電流値制御により、上述のように銀イオン濃度を一定とすることができる。また銀イオン濃度を任意に制御することが可能となる。
【0010】
なお、供給制御装置3により流量カウンタ5からの流量信号に基づいて流量累積値を求め、所定値に達したら電流値制御装置30に信号を送り所定時間銀イオンを供給することにより間欠的に銀イオンの供給を行わせる。
【0011】
次に実施形態の動作を説明する。
図2において供給制御装置3は流量カウンタ5からの値を検出及び積算し(ステップS10)、累積値が所定値になったら(ステップS11)、同様に電流値を計算し(ステップS12)、電流値制御装置30に信号を送り、該電流値に基づいて銀電極6と不溶解電極7に通電する(ステップS13)。所定時間通電したら(ステップS14)、電流を停止して(ステップS15)、ステップS10に戻る。
以上の動作により、常に一定量の銀イオンを間欠的に供給がすることができる。
【001
以上説明した実施形態によれば、浄水器或いは整水器等において一定濃度の銀イオンを供給することができ、本体や濾材に残留水や滞留水中の細菌の増殖を抑制することができる。また間欠的な駆動も正確に行えるから、効率的な抗菌作用を適正に維持することが可能になる。
【001
【発明の効果】
以上説明したように本発明の水処理装置によれば、細菌の増殖を抑制できる効果がある。
【図面の簡単な説明】
【図1】本発明の一実施形態を示す概略図。
【図】本発明の一実施形態の他の動作を示すフローチャート図。
【符号の説明】
1:銀イオン供給装置、3:供給制御装置、5:流量カウンタ、6:銀電極、7:不溶解電極、8:銀溶解槽、10:浄水カートリッジ、30:電流値制御装置。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a water treatment apparatus such as a water conditioner or a water purifier.
[0002]
[Prior art]
In the water conditioner and the water purifier, activated carbon or the like is used as a filter medium to treat residual chlorine, organic matter, and the like in tap water. Since the residual chlorine, which is a disinfectant, has been removed from the water after passing through the filter medium by this activated carbon, the remaining water in the filter medium and the residual water remaining in the container when the water conditioner and water purifier are not used for a long time. There is a problem that bacteria in the water grow. In general, in order to suppress the growth of bacteria, a method using antibacterial activated carbon with silver attached as activated carbon in the filter medium is used. When this antibacterial activated carbon comes into contact with water, it elutes silver ions, and the silver ions can suppress bacterial growth.
[0003]
[Problems to be solved by the invention]
However, antibacterial activated carbon impregnated with silver has a silver ion elution period of about several days, and it is difficult to suppress bacterial growth in the residual water inside the filter medium and the residual water remaining in the main body for a long time. is there.
The object of the present invention is to solve the problems of the prior art.
[0004]
[Means for Solving the Problems]
In order to achieve the above object, the present invention provides a water treatment apparatus including a filter medium,
A means for supplying silver ions by electrolysis of silver provided upstream of the filter medium, a flow rate detecting means for detecting a flow rate of the supplied water supplied to the water treatment device, and a flow rate of the supplied water from the flow rate detecting means. And a control means for controlling the amount of silver electrolysis by controlling the current for electrolysis of the silver, and the control means intermittently supplies silver ions by the means for supplying silver ions. The problem was solved by using a water treatment device that was controlled to supply.
The silver ions can suppress the growth of bacteria in the residual water in the water treatment apparatus and the retained water of the filter medium. Moreover, since the flow rate of the feed water can be detected and the amount of silver ions delivered can be controlled based on this, an appropriate antibacterial action can always be obtained.
By supplying silver ions from the means for supplying silver ions, the silver ions are adsorbed on the downstream filter medium and gradually dissolved in water from the filter medium, so that a continuous effect can be obtained.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below with reference to the drawings.
[0006]
FIG. 1 shows one embodiment.
In FIG. 1, supply water such as tap water is supplied to the water purification cartridge 10 from upstream, and the supply water is purified by a filter medium such as activated carbon stored in the water purification cartridge 10 to flow downstream.
A silver ion supply device 1 is provided on the upstream side of the water purification cartridge 10, and silver ions are added to the supply water continuously or intermittently. The silver ions added to the supply water are adsorbed by the filter medium (activated carbon etc.) of the water purification cartridge 10 and maintain the antibacterial action for a predetermined time even after the supply of silver ions from the silver ion supply device 1 is stopped. Yes.
[0007]
The silver ion supply device 1 is a supply device by electrolysis of silver, and has a structure in which a silver dissolution tank 8 is provided with a silver electrode 6 as an anode and an insoluble electrode 7 as a cathode. Silver ions are supplied into the supply water by energizing the electrodes 6 and 7 every predetermined time. Platinum, gold, carbon rod, SUS, Ti, Ti—Pt can be used as the insoluble electrode 7.
The elution amount of silver ions is determined by Faraday's law as shown below. Therefore, the silver ion concentration of the feed water by the addition of silver ions can be made constant by detecting the flow rate of the feed water and controlling the current value flowing between the silver electrode and the insoluble electrode according to the detected value. it can. In addition, an arbitrary concentration can be obtained by current value control.
Elution amount of silver (g) = 1 gram equivalent of silver (g) x {current value (A) x time (sec) ÷ 96500 (q)}
Concentration of silver in feed water (g / L) = 1 gram equivalent of silver (g) x
{Current value (A) ÷ (96500 (q) x Flow rate (L / sec))}
[0009]
In order to detect the flow rate, a flow rate counter 5 is provided in the flow path of the supply water. In this embodiment, a flow rate counter 5 is provided between the silver ion supply device 1 and the water purification cartridge 10 to send a flow rate signal to the supply control device 3.
The supply control device 3 obtains a current value according to the above formula based on the flow rate signal from the flow rate counter 5, and controls the current value supplied to the silver electrode 6 and the insoluble electrode 7 via the current value control device 30. ing. By this current value control, the silver ion concentration can be made constant as described above. In addition, the silver ion concentration can be arbitrarily controlled.
[0010]
The supply control device 3 obtains a cumulative flow rate value based on the flow rate signal from the flow rate counter 5, and when it reaches a predetermined value, it sends a signal to the current value control device 30 to supply silver ions for a predetermined time, thereby intermittently silvering. Ru to perform the supply of the ion.
[0011]
Then explaining the operation of the embodiment.
In FIG. 2 , the supply control device 3 detects and integrates the value from the flow rate counter 5 (step S10). When the accumulated value reaches a predetermined value (step S11), the current value is similarly calculated (step S12). A signal is sent to the value control device 30, and the silver electrode 6 and the insoluble electrode 7 are energized based on the current value (step S13). When energized for a predetermined time (step S14), the current is stopped (step S15), and the process returns to step S10.
By the above operation, a constant amount of silver ions can be supplied intermittently.
[001 2 ]
According to the embodiment described above, silver ions having a constant concentration can be supplied in a water purifier, a water conditioner, or the like, and bacterial growth in residual water or stagnant water can be suppressed on the main body or filter medium. In addition, since intermittent driving can be performed accurately, efficient antibacterial action can be properly maintained.
[001 3 ]
【The invention's effect】
As described above, according to the water treatment apparatus of the present invention, there is an effect of suppressing the growth of bacteria.
[Brief description of the drawings]
FIG. 1 is a schematic view showing an embodiment of the present invention.
FIG. 2 is a flowchart showing another operation of the embodiment of the present invention.
[Explanation of symbols]
1: Silver ion supply device, 3: Supply control device, 5: Flow rate counter, 6: Silver electrode, 7: Insoluble electrode, 8: Silver dissolution tank, 10: Water purification cartridge, 30: Current value control device.

Claims (1)

濾材を備えた水処理装置において、
濾材の上流側に備えられた銀の電解により銀イオンを供給する手段と、
水処理装置に供給される供給水の流量を検出する流量検出手段と、
前記流量検出手段からの供給水の流量に基づいて、前記銀の電解のための電流を制御することにより、銀の電解量を制御する制御手段と、を備え、
該制御手段は前記銀イオンを供給する手段による銀イオンの供給を間欠的に供給するように制御する、
ことを特徴とする水処理装置。
In a water treatment device equipped with a filter medium,
Means for supplying silver ions by electrolysis of silver provided upstream of the filter medium;
Flow rate detection means for detecting the flow rate of the feed water supplied to the water treatment device;
Control means for controlling the amount of electrolyzed silver by controlling the current for electrolysis of silver based on the flow rate of the supply water from the flow rate detecting means,
The control means controls the supply of silver ions by the means for supplying silver ions to be intermittently supplied.
The water treatment apparatus characterized by the above-mentioned.
JP14322799A 1999-05-24 1999-05-24 Water treatment equipment Expired - Fee Related JP4267755B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14322799A JP4267755B2 (en) 1999-05-24 1999-05-24 Water treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14322799A JP4267755B2 (en) 1999-05-24 1999-05-24 Water treatment equipment

Publications (2)

Publication Number Publication Date
JP2000325953A JP2000325953A (en) 2000-11-28
JP4267755B2 true JP4267755B2 (en) 2009-05-27

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JP14322799A Expired - Fee Related JP4267755B2 (en) 1999-05-24 1999-05-24 Water treatment equipment

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010085036A (en) * 2001-07-24 2001-09-07 김유창 Apparatus and method for removing an industrial pollution material by copper and silver ion
JP3957619B2 (en) 2002-11-22 2007-08-15 シャープ株式会社 Ion elution unit and equipment equipped with the same
JP4129736B2 (en) * 2003-03-05 2008-08-06 株式会社安川電機 Water purifier
KR100845955B1 (en) 2007-05-04 2008-07-11 (주) 테크윈 Electrolytic Sterilizer with Insoluble Electrode Filling Layer
JP2013015305A (en) * 2011-07-06 2013-01-24 Toshiba Carrier Corp Hot water supply apparatus
JP5315470B1 (en) * 2013-03-01 2013-10-16 稲森 總一郎 Electrolysis device, ice making device and ice making method

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