JP2000325953A - Water treatment apparatus - Google Patents
Water treatment apparatusInfo
- Publication number
- JP2000325953A JP2000325953A JP11143227A JP14322799A JP2000325953A JP 2000325953 A JP2000325953 A JP 2000325953A JP 11143227 A JP11143227 A JP 11143227A JP 14322799 A JP14322799 A JP 14322799A JP 2000325953 A JP2000325953 A JP 2000325953A
- Authority
- JP
- Japan
- Prior art keywords
- silver
- water
- supplied
- silver ions
- filter material
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 229910052709 silver Inorganic materials 0.000 claims abstract description 49
- 239000004332 silver Substances 0.000 claims abstract description 49
- -1 silver ions Chemical class 0.000 claims abstract description 26
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 6
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 6
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 abstract description 13
- 241000894006 Bacteria Species 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract 4
- 230000005684 electric field Effects 0.000 abstract 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 17
- 239000008400 supply water Substances 0.000 description 8
- 230000000844 anti-bacterial effect Effects 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 239000000460 chlorine Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 102100033041 Carbonic anhydrase 13 Human genes 0.000 description 1
- 102100029774 Eukaryotic translation initiation factor 1b Human genes 0.000 description 1
- 101000867860 Homo sapiens Carbonic anhydrase 13 Proteins 0.000 description 1
- 101001012792 Homo sapiens Eukaryotic translation initiation factor 1b Proteins 0.000 description 1
- 229910003086 Ti–Pt Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000002844 continuous effect Effects 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Water Treatment By Sorption (AREA)
Abstract
Description
【0001】[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。The present invention relates to a water treatment device such as a water purifier or a water purifier.
【0002】[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。2. Description of the Related Art In a water purifier and a water purifier, activated carbon or the like is used as a filter medium for treating residual chlorine, organic substances, and the like in tap water. Since residual chlorine as a disinfectant has been removed from the water after passing through the filter media by this activated carbon, etc., if the water conditioner and water purifier are not used for a long time, the residual water inside the filter media and the residual There is a problem that bacteria in water grow. Generally, a method of using antibacterial activated carbon to which silver is attached as activated carbon in a filter medium is used to suppress the growth of the bacteria. This antibacterial activated carbon elutes silver ions when it comes into contact with water, and the silver ions can suppress the growth of bacteria.
【0003】[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。However, in the antibacterial activated carbon impregnated with silver, the elution period of the silver ion is about several days, and the bacteria in the residual water in the filter medium and the residual water remaining in the main body for a long period of time. There is a problem that growth cannot be suppressed. An object of the present invention is to solve the above-mentioned problems of the prior art.
【0004】[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、前記銀の電解量を制御する制御手段とを備えた
ことを特徴とする。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は、連
続的であっても良いし或いは間欠的であっても良い。間
欠的であっても、下流側の濾材に吸着され、濾材から少
しづつ水の中に溶け出すため、連続的な効果が得られ
る。In order to achieve the above object, the present invention provides a water treatment apparatus provided with a filter medium, comprising means for supplying silver ions by electrolysis of silver provided on the upstream side of the filter medium; Control means for controlling the amount of silver electrolysis. The silver ions make it possible to suppress the growth of bacteria in the residual water in the water treatment apparatus and in the stagnant water of the filter medium. In addition, since the amount of silver ions supplied can be controlled, an appropriate antibacterial action can always be obtained.
The supply of silver ions from the means for supplying silver ions may be continuous or intermittent. Even if it is intermittent, it is adsorbed by the filter medium on the downstream side and gradually dissolves out of water from the filter medium, so that a continuous effect can be obtained.
【0005】[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。Embodiments of the present invention will be described below with reference to the drawings.
【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。FIG. 1 shows one embodiment. In FIG. 1, supply water such as tap water is supplied to the water purification cartridge 10 from the upstream, and the supply water is purified by a filter medium such as activated carbon housed in the water purification cartridge 10 and is then flowed downstream. A silver ion supply device 1 is provided on the upstream side of the water purification cartridge 10 so that silver ions are added to supply water continuously or intermittently. The silver ions added to the supply water are adsorbed on the filter medium (eg, activated carbon) of the water purification cartridge 10, and the antibacterial action is maintained for a predetermined time even after the supply of silver ions from the silver ion supply device 1 is stopped. I have.
【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、T
i、Ti−Ptを用いることが可能であるThe silver ion supply device 1 is a supply device using silver electrolysis, and a silver dissolving tank 8 has a silver electrode 6 serving as an anode.
And an insoluble electrode 7 as a cathode. By supplying electricity to the electrodes 6 and 7 at predetermined time intervals, silver ions are supplied into the supply water.
Platinum, gold, carbon rod, SUS, T
i, Ti-Pt can be used
【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))}The amount of silver ion eluted is determined by Faraday's law shown in the following equation. Therefore, the silver ion concentration of the supply water due to the addition of silver ions can be made constant by detecting the flow rate of the supply water and controlling the current value flowing between the silver electrode and the insoluble electrode according to the detected value. it can. Also, an arbitrary concentration can be obtained by controlling the current value. Silver elution amount (g) = 1 gram equivalent of silver (g) x {current value (A) x
Time (sec) ÷ 96500 (q) 濃度 Silver concentration in feed water (g / L) = 1 gram equivalent of silver (g) × {current value (A) ÷ (96500 (q) × flow rate (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。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 counter 5 is provided between the silver ion supply device 1 and the water purification cartridge 10, and sends a flow signal to the supply control device 3. The supply control device 3 obtains a current value according to the above equation based on the flow signal from the flow 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 kept constant as described above. Further, the silver ion concentration can be arbitrarily controlled.
【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
行わせることも可能である。The supply controller 3 calculates an accumulated flow value based on a flow signal from the flow counter 5 and, when the accumulated value reaches a predetermined value, sends a signal to the current value control device 30 to supply silver ions for a predetermined time, thereby intermittently. It is also possible to supply silver ions specifically.
【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からの流量を検
出し(ステップS1)、該検出値に基づいて所定の銀イ
オンを供給する電流値を計算する(ステップS2)。そ
して電流値制御装置30を介して銀電極6と不溶解電極
7へ通電し、ステップS1に戻る。以上の動作により、
銀イオン供給装置1からは正確な量の銀イオンの供給が
行われる。Next, the operation of the embodiment will be described. In FIG. 2, the supply control device 3 detects the flow rate from the flow counter 5 (step S1), and calculates a current value for supplying predetermined silver ions based on the detected value (step S2). Then, current is supplied to the silver electrode 6 and the insoluble electrode 7 via the current value control device 30, and the process returns to step S1. By the above operation,
The silver ion supply device 1 supplies an accurate amount of silver ions.
【0012】次に間欠供給動作を説明する。図3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。Next, the intermittent supply operation will be described. In FIG. 3, the supply control device 3 detects and integrates the value from the flow counter 5 (step S10), and when the accumulated value reaches a predetermined value (step S11), similarly calculates the current value (step S12). A signal is sent to the value controller 30, and the silver electrode 6 and the insoluble electrode 7 are energized based on the current value (step S13). After energizing for a predetermined time (step S14),
The current is stopped (step S15), and the process returns to step S10. With the above operation, a constant amount of silver ions can be constantly supplied intermittently.
【0013】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。According to the embodiment described above, it is possible to supply silver ions at a constant concentration in a water purifier, a water purifier, or the like, and to suppress the growth of bacteria in residual water or retained water in the main body or the filter medium. it can. In addition, since intermittent driving can be performed accurately, efficient antibacterial action can be appropriately maintained.
【0014】[0014]
【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。As described above, according to the water treatment apparatus of the present invention, there is an effect that the growth of bacteria can be suppressed.
【図1】本発明の一実施形態を示す概略図。FIG. 1 is a schematic diagram showing an embodiment of the present invention.
【図2】本発明の一実施形態の動作を示すフローチャー
ト図。FIG. 2 is a flowchart showing the operation of one embodiment of the present invention.
【図3】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。FIG. 3 is a flowchart showing another operation of the embodiment of the present invention.
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。1: silver ion supply device, 3: supply control device, 5: flow counter, 6: silver electrode, 7: insoluble electrode, 8: silver dissolution tank,
10: water purification cartridge, 30: current value control device.
───────────────────────────────────────────────────── 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 1/50 540 C02F 1/50 540B 550 550D 550L 560 560F (72)発明者 仲 村 恵 理 子 東京都八王子市狭間町1463番地 蛇の目ミ シン工業株式会社内 Fターム(参考) 4D024 AA02 AB07 BA02 CA13 DA03 DB27 4D061 DA03 DB01 DB09 EA03 EB02 EB04 EB30 EB31 EB37 EB39 FA06 GA02 GC02 GC12 GC20──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) C02F 1/50 540 C02F 1/50 540B 550 550D 550L 560 560F (72) Inventor: Eriko Nakamura Tokyo 1463, Hazama-cho, Hachioji, Japan F-term (reference) 4J024 AA02 AB07 BA02 CA13 DA03 DB27 4D061 DA03 DB01 DB09 EA03 EB02 EB04 EB30 EB31 EB37 EB39 FA06 GA02 GC02 GC12 GC20
Claims (3)
給する手段と、 前記銀の電解量を制御する制御手段と、 を備えたことを特徴とする水処理装置。1. A water treatment apparatus provided with a filter medium, comprising: means for supplying silver ions by electrolysis of silver provided upstream of the filter medium; and control means for controlling the amount of silver electrolysis. A water treatment apparatus characterized by the above-mentioned.
ンを連続的に供給する、 請求項1に記載の水処理装置。2. The water treatment apparatus according to claim 1, wherein the means for supplying silver ions continuously supplies silver ions.
ンを間欠的に供給する、 請求項1に記載の水処理装置。3. The water treatment apparatus according to claim 1, wherein the means for supplying silver ions supplies silver ions intermittently.
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 true JP2000325953A (en) | 2000-11-28 |
| JP4267755B2 JP4267755B2 (en) | 2009-05-27 |
Family
ID=15333867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14322799A Expired - Fee Related JP4267755B2 (en) | 1999-05-24 | 1999-05-24 | Water treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP4267755B2 (en) |
Cited By (6)
| 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 |
| JP2004267819A (en) * | 2003-03-05 | 2004-09-30 | Yaskawa Electric Corp | Water purification equipment |
| 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 |
| US8448479B2 (en) | 2002-11-22 | 2013-05-28 | Sharp Kabushiki Kaisha | Ion eluting unit and device loaded with same |
| JP5315470B1 (en) * | 2013-03-01 | 2013-10-16 | 稲森 總一郎 | Electrolysis device, ice making device and ice making method |
-
1999
- 1999-05-24 JP JP14322799A patent/JP4267755B2/en not_active Expired - Fee Related
Cited By (6)
| 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 |
| US8448479B2 (en) | 2002-11-22 | 2013-05-28 | Sharp Kabushiki Kaisha | Ion eluting unit and device loaded with same |
| JP2004267819A (en) * | 2003-03-05 | 2004-09-30 | Yaskawa Electric Corp | Water purification equipment |
| 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 |
Also Published As
| Publication number | Publication date |
|---|---|
| JP4267755B2 (en) | 2009-05-27 |
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