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JPS6356942B2 - - Google Patents
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JPS6356942B2 - - Google Patents

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Publication number
JPS6356942B2
JPS6356942B2 JP56058775A JP5877581A JPS6356942B2 JP S6356942 B2 JPS6356942 B2 JP S6356942B2 JP 56058775 A JP56058775 A JP 56058775A JP 5877581 A JP5877581 A JP 5877581A JP S6356942 B2 JPS6356942 B2 JP S6356942B2
Authority
JP
Japan
Prior art keywords
water
activated carbon
filter
desalination
chlorine
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
Application number
JP56058775A
Other languages
Japanese (ja)
Other versions
JPS57172244A (en
Inventor
Toshio Shirota
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.)
Kotobuki Kogyo KK
Original Assignee
Kotobuki Kogyo KK
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 Kotobuki Kogyo KK filed Critical Kotobuki Kogyo KK
Priority to JP56058775A priority Critical patent/JPS57172244A/en
Publication of JPS57172244A publication Critical patent/JPS57172244A/en
Publication of JPS6356942B2 publication Critical patent/JPS6356942B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/26Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
    • G01N27/416Systems
    • G01N27/4166Systems measuring a particular property of an electrolyte
    • G01N27/4168Oxidation-reduction potential, e.g. for chlorination of water

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Molecular Biology (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Measuring Oxygen Concentration In Cells (AREA)
  • Water Treatment By Sorption (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は脱塩素装置における残留塩素漏洩にと
もなう脱塩素材の交換時期を適切に検知するため
の脱塩素装置における脱塩素材の交換時期検出装
置に関する。 従来、例えば一般家庭等に供給される水道の水
から殺菌用塩素分を除去するための装置として脱
塩素装置、即ち、活性炭を脱塩素材とする脱塩素
フイルタ中に水道の水を通して、水に含まれる塩
素分を活性炭に吸着及び触媒作用により除去する
脱塩素装置が用いられ、かつ、活性炭は脱塩作用
がなくなる前に早期に交換するようにしている。 そこで、活性炭交換時期に対応した脱塩素装置
の活性炭終点検知方法としては、例えば、脱塩素
装置からの処理済水にO―トリジン塩酸塩溶液を
加えたことによる残留塩素との反応にともなう着
色によつて活性炭の終点を検知しているが、この
場合、肉眼での着色の有無の判断によつて残留塩
素漏洩を確認することから、漏洩濃度が低濃度の
場合には特にその着色判断が困難である他、この
終点検知に用いられるO―トリジン塩酸塩溶液は
発がん性のおそれのある物質として法的規制の対
象となつているという云う欠点がある。 又、これに代わる活性炭の終点検知方法として
は、例えば活性炭の通水倍率による終点検知の方
法があるが、この場合、原水の残留塩素濃度及び
通水流速によつて活性炭の終点時期が大幅に変動
するため、活性炭の終点時期を正確に検知するこ
とができないと云う欠点があつた。 本発明の目的は無試薬でしかも原水中に含まれ
るFeイオン、Cuイオン等の妨害イオン及びPH等
に影響されることなく脱塩素装置における活性炭
等脱塩素材の交換時期を適切に検出する方法を提
供することによつて、前記従来の欠点を除去する
ことにある。 次に、本発明の一実施例の構成を図面によつて
説明する。 脱塩素装置1の円筒状フイルタ容器2上端には
被処理用原水の例えば水道の水を供給する流入パ
イプ3が接続され、その下端部には脱塩素処理さ
れた水を各蛇口等に供給する流出パイプ4が接続
され、かつ、フイルタ容器2の内部は円筒状連通
パイプ5の外周に形成したフランジ状セパレータ
6を介して上部、中間部、下部の3つのフイルタ
室7,8,9に分割され、各フイルタ室7,8,
9には原子中の塩素分を除去する活性炭10がフ
イルタ素材として充填されている。 又、フイルタ容器2の下端部から連通パイプ5
内軸心上に挿着された電気絶縁材料製絶縁ロツド
11の中間部と下端部には連通パイプ5の流路を
遮断する遮蔽リング12が取付けられ、同リング
12で2分された連通パイプ5の各連通路13,
14には各フイルタ室7,8,9と接する位置に
おいて連通孔15が形成されている他、絶縁ロツ
ド11の各連通路13,14位置にはメツキを含
む銀製電極16と銀よりイオン化傾向の小さい貴
金属、例えば白金若しくは金製電極17が1対の
ガルバーニ電極18,19として取付けられてい
る。 従つて、このように構成された脱塩素装置1の
フイルタ容器2に流入パイプ3を介して原水が供
給されると、同原水はサラン(商品名)ネツトの
網状フイルタ20を介して異物が除去された状態
で上部フイルタ室7から連通パイプ5の上部連通
路13、中間部フイルタ室8、連通パイプ5の下
部連通路14、下部フイルタ室9、活性炭10流
出防止用サランネツトの網状フイルタ21を通つ
て流出パイプ4から蛇口等に供給されるととも
に、この通水状態において、各連通路13,14
の電極18,19からは各連通路13,14を通
る水を電解液としたガルバーニ起電圧が発生し、
同起電圧は、電極棒11内を通つて各電極16,
17に接続された電線22を介して外部の検出装
置23に入力される。 次に、第2図は本実施例の電気回路であつて、
006P―9Vの電源電池Bから電源スイツチSW1、
プラス電位安定用とマイナス電位安定用各抵抗R
1,R2、ツエナーダイオードZD1,ZD2、ダ
イオードD1,D2、コンデンサC1,C2を介
して電源が供給される差動増幅器AMP1は可変
抵抗VR1を介してオフセツト調整されるととも
に、その非反転側入力端子には上流側電極18か
らのガルバニー電圧が入力抵抗R3を介して入力
され、その反対側入力端子には下流側電極19か
らのガルバーニ起電圧が入力抵抗R4を介して入
力され、差動増幅器AMP1からは前記入力抵抗
R3,R4と帰環抵抗R5,R6とで定まる増幅
率と入力電圧の差に対応した出力が発生するとと
もに、差動増幅器AMP1からの出力はダイオー
ドD3、可変抵抗VR2、切換スイツチSW2を
介して電流計Mに入力される他、電流計Mは切換
スイツチSW2を介して電源電池Bチエツク用抵
抗Rに接続され、差動増幅器AMP1の出力端子
にはプルアツプ用抵抗R8が接続されている。 次に、本実施例の作用について説明する。 まず、差動増幅器AMP1の反転及び非反転側
入力がともに零の状態において電流計Mの指針が
零レンジを示すように可変抵抗VR1を介してオ
フセツト調整した状態で、脱塩素装置1に殺菌用
塩素を含む水道の水を原水として通水すると、原
水中の塩素はまず、活性炭に吸着され、その触媒
作用により 2Cl2+2H2O4Hcl+O2 ……(1) の反応を起こして、活性炭10による脱塩素の吸
着帯が形成されるが、この通水初期において、上
部フイルタ室7から上部連通路13に流れ込む処
理済水中には残留塩素の漏洩が殆どなく、従つ
て、上流及び下流のガルバーニ電極18,19
は、ともにほぼ同一起電圧を発生していることか
ら差動増幅器AMP1の出力はほぼ零で、電流計
Mの指示値も零のまま変化しない。 なお、この通水状態の原水中に妨害イオンの
Fe+等が含まれていても、これ等妨害イオンは空
間速度SVが実用のSV30以上においては活性炭1
0に殆ど吸着されないことから上流・下流各ガル
バーニ電極18,19の起電圧は、ともに妨害イ
オンの程度に対応してほぼ同程度に上昇するた
め、差動増幅器AMP1の出力は妨害イオンによ
つても変化せず零のままで、電流計Mの指針も零
のまま変わらず、従つて、電流計Mが妨害イオン
によつて誤動作することはない。 次に、原水の活性炭10内通水にともない原水
中の塩素は活性炭10に吸着され前記(1)式の反応
により、原水中の塩素2Cl2が4HClとなつて脱塩
素の吸着帯が形成される他、通水時間の経過に従
つて前記吸着帯が下流に移動し、この吸着帯が上
部フイルタ室7から中部フイルタ室8に移動する
時点においては、上部連通路13の被検水中に残
留塩素が漏洩しはじめるとともに、この漏洩量は
時間の経過に従つて次第に増大して被検水中の残
留塩素濃度が原水濃度に近づき、この状態におい
て被検水、この場合、漏洩水中の残留塩素はそれ
ぞれ上部連通路13中ガルバーニ電極18の銀電
極16と白金電極17上で
The present invention relates to a replacement time detection device for a desalination material in a dechlorination device for appropriately detecting the time to replace the desalination material due to residual chlorine leakage in the dechlorination device. Conventionally, as a device for removing sterilizing chlorine from tap water supplied to general households, for example, a dechlorination device, that is, a dechlorination filter using activated carbon as the desalting material, is used to pass tap water through a filter. A dechlorination device is used that removes the chlorine content through adsorption and catalytic action on activated carbon, and the activated carbon is replaced as soon as possible before it loses its desalination effect. Therefore, as a method for detecting the end point of activated carbon in a dechlorination equipment corresponding to the timing of activated carbon replacement, for example, the coloring due to the reaction with residual chlorine caused by adding O-tolidine hydrochloride solution to the treated water from the dechlorination equipment can be used. Therefore, the end point of activated carbon is detected, but in this case, residual chlorine leakage is confirmed by determining the presence or absence of coloration with the naked eye, so it is difficult to determine the coloration, especially when the leakage concentration is low. Another drawback is that the O-tolidine hydrochloride solution used for this end point detection is subject to legal regulation as a potentially carcinogenic substance. In addition, as an alternative method for detecting the end point of activated carbon, for example, there is a method of detecting the end point by the water flow rate of activated carbon. This has the disadvantage that it is not possible to accurately detect the end point of activated carbon because of fluctuations. The purpose of the present invention is to appropriately detect when to replace desalination materials such as activated carbon in a dechlorination equipment without using reagents and without being affected by interfering ions such as Fe ions and Cu ions and pH contained in raw water. The object of the present invention is to eliminate the above-mentioned drawbacks of the prior art. Next, the configuration of an embodiment of the present invention will be explained with reference to the drawings. An inflow pipe 3 for supplying raw water to be treated, such as tap water, is connected to the upper end of the cylindrical filter container 2 of the dechlorinator 1, and the lower end thereof supplies dechlorinated water to each faucet. The outflow pipe 4 is connected, and the inside of the filter container 2 is divided into three filter chambers 7, 8, and 9, an upper, middle, and lower part, via a flange-like separator 6 formed on the outer periphery of the cylindrical communication pipe 5. and each filter chamber 7, 8,
9 is filled with activated carbon 10 as a filter material, which removes chlorine from atoms. Also, a communicating pipe 5 is connected to the lower end of the filter container 2.
A shielding ring 12 for blocking the flow path of the communicating pipe 5 is attached to the middle and lower end of the insulating rod 11 made of an electrically insulating material inserted on the inner axis, and the communicating pipe is divided into two by the ring 12. 5 each communication path 13,
Communication holes 15 are formed in the insulating rod 11 at positions in contact with the filter chambers 7, 8, and 9, and silver electrodes 16 containing plating are formed in the communication passages 13 and 14 of the insulating rod 11. A small noble metal electrode 17, for example platinum or gold, is mounted as a pair of galvanic electrodes 18,19. Therefore, when raw water is supplied to the filter container 2 of the dechlorination apparatus 1 configured as described above through the inflow pipe 3, foreign substances are removed from the raw water through the mesh filter 20 of Saran (trade name) Net. In this state, the activated carbon 10 is passed through the upper communication passage 13 of the communication pipe 5, the intermediate filter chamber 8, the lower communication passage 14 of the communication pipe 5, the lower filter chamber 9, and the mesh filter 21 of the saran net for preventing the activated carbon 10 from flowing out. The water is supplied from the outflow pipe 4 to a faucet etc., and in this state of water flow, each communication passage 13, 14
A galvanic electromotive force is generated from the electrodes 18 and 19 using water as an electrolyte passing through each communication path 13 and 14,
The same electromotive voltage passes through the electrode rod 11 to each electrode 16,
The signal is inputted to an external detection device 23 via an electric wire 22 connected to a terminal 17. Next, FIG. 2 shows the electric circuit of this embodiment,
006P-9V power supply battery B to power switch SW1,
Each resistor R for positive potential stabilization and negative potential stabilization
1, R2, Zener diodes ZD1, ZD2, diodes D1, D2, and capacitors C1, C2. The differential amplifier AMP1 is offset-adjusted via a variable resistor VR1, and its non-inverting side input terminal The galvanic voltage from the upstream electrode 18 is inputted to the input terminal via the input resistor R3, and the galvanic electromotive force from the downstream electrode 19 is inputted to the input terminal on the opposite side via the input resistor R4. An output corresponding to the difference between the input voltage and the amplification factor determined by the input resistors R3, R4 and the return resistors R5, R6 is generated, and the output from the differential amplifier AMP1 is connected to the diode D3, the variable resistor VR2, and the switching In addition to being input to the ammeter M via the switch SW2, the ammeter M is also connected to the power supply battery B check resistor R via the changeover switch SW2, and the pull-up resistor R8 is connected to the output terminal of the differential amplifier AMP1. has been done. Next, the operation of this embodiment will be explained. First, when the inverting and non-inverting side inputs of the differential amplifier AMP1 are both zero, the offset is adjusted via the variable resistor VR1 so that the pointer of the ammeter M indicates the zero range, and then the dechlorinator 1 is connected to the sterilizer. When tap water containing chlorine is passed through as raw water, the chlorine in the raw water is first adsorbed by activated carbon, and its catalytic action causes the reaction 2Cl 2 + 2H 2 O4Hcl + O 2 ...(1), which is desorbed by activated carbon 10. Although a chlorine adsorption zone is formed, there is almost no leakage of residual chlorine in the treated water flowing from the upper filter chamber 7 to the upper communication passage 13 at this early stage of water flow, and therefore the upstream and downstream galvanic electrodes 18 ,19
Since both generate substantially the same electromotive voltage, the output of the differential amplifier AMP1 is substantially zero, and the indicated value of the ammeter M also remains zero and does not change. Note that there are no interfering ions in the raw water under this condition.
Even if Fe + etc. are included, these interfering ions can be absorbed by activated carbon at a space velocity of SV30 or more.
0, the electromotive voltages of the upstream and downstream galvanic electrodes 18 and 19 both rise to approximately the same degree in response to the degree of interfering ions, so the output of the differential amplifier AMP1 depends on the interfering ions. does not change and remains at zero, and the pointer of the ammeter M also remains at zero, so that the ammeter M will not malfunction due to interfering ions. Next, as the raw water passes through the activated carbon 10, the chlorine in the raw water is adsorbed by the activated carbon 10, and due to the reaction of equation (1), the chlorine 2Cl 2 in the raw water becomes 4HCl, forming a dechlorination adsorption zone. In addition, as the water flow time elapses, the adsorption zone moves downstream, and at the time when this adsorption zone moves from the upper filter chamber 7 to the middle filter chamber 8, there is no residue remaining in the test water in the upper communication passage 13. As chlorine begins to leak, the leakage amount gradually increases over time, and the residual chlorine concentration in the test water approaches the raw water concentration.In this state, the residual chlorine in the test water, in this case the leaked water, is on the silver electrode 16 and platinum electrode 17 of the galvanic electrode 18 in the upper communication path 13, respectively.

【表】 1
〓HOCl+e
[Table] 1
〓HOCl+e

Claims (1)

【特許請求の範囲】[Claims] 1 被処理水を通水させる脱塩素材のフイルタ中
におけるフイルタ素材の脱塩素材室を少なくとも
3室に分割し、各脱塩素材室を少なくとも2路の
連通路で直列に連通するとともに、該少なくとも
2路の連通路に前記被処理水を電解液とする一対
の電極を取付け、かつ、残留塩素漏洩にともなう
脱塩素材交換時期検出に対応して各連通路に形成
された前記各電極別起電圧の差を検出する起電圧
差検出回路を備えることを特徴とする脱塩素装置
における脱塩素材交換時期検出装置。
1 The desalination material chamber of the filter material in the filter of the desalination material through which the water to be treated passes is divided into at least three chambers, and each desalination material chamber is connected in series with at least two communication paths, and A pair of electrodes using the water to be treated as an electrolyte is attached to at least two communication paths, and each electrode is separately formed in each communication path in order to detect the time to replace desalination material due to leakage of residual chlorine. A desalination material replacement timing detection device in a dechlorination equipment, characterized by comprising an electromotive force difference detection circuit that detects a difference in electromotive force.
JP56058775A 1981-04-16 1981-04-16 Detecting method for exchange time of dechlorination material of dechlorination apparatus Granted JPS57172244A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56058775A JPS57172244A (en) 1981-04-16 1981-04-16 Detecting method for exchange time of dechlorination material of dechlorination apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56058775A JPS57172244A (en) 1981-04-16 1981-04-16 Detecting method for exchange time of dechlorination material of dechlorination apparatus

Publications (2)

Publication Number Publication Date
JPS57172244A JPS57172244A (en) 1982-10-23
JPS6356942B2 true JPS6356942B2 (en) 1988-11-09

Family

ID=13093918

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56058775A Granted JPS57172244A (en) 1981-04-16 1981-04-16 Detecting method for exchange time of dechlorination material of dechlorination apparatus

Country Status (1)

Country Link
JP (1) JPS57172244A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0347649A (en) * 1989-07-13 1991-02-28 Toyota Motor Corp Metallic mold for casting

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61136487A (en) * 1984-12-06 1986-06-24 Hitachi Ltd Water purifier
FR2576416B1 (en) * 1985-01-23 1988-03-04 Socea Balency METHOD AND APPARATUS FOR CONTINUOUS OR SEQUENTIAL MEASUREMENT OF THE HALOGEN CONCENTRATION OF AQUEOUS SOLUTIONS
JPH0422875Y2 (en) * 1985-05-10 1992-05-26
WO2005047880A1 (en) * 2003-11-14 2005-05-26 Tanita Corporation Water examiner
US8025779B2 (en) 2003-11-14 2011-09-27 Tanita Corporation Water quality analyzer

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4936395A (en) * 1972-08-05 1974-04-04

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0347649A (en) * 1989-07-13 1991-02-28 Toyota Motor Corp Metallic mold for casting

Also Published As

Publication number Publication date
JPS57172244A (en) 1982-10-23

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