JPS5934964B2 - Electrode type sludge interface meter - Google Patents
Electrode type sludge interface meterInfo
- Publication number
- JPS5934964B2 JPS5934964B2 JP52014593A JP1459377A JPS5934964B2 JP S5934964 B2 JPS5934964 B2 JP S5934964B2 JP 52014593 A JP52014593 A JP 52014593A JP 1459377 A JP1459377 A JP 1459377A JP S5934964 B2 JPS5934964 B2 JP S5934964B2
- Authority
- JP
- Japan
- Prior art keywords
- pair
- sludge
- detection electrodes
- electrode
- interface meter
- 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
Links
Landscapes
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
- Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)
Description
【発明の詳細な説明】
本発明は、電気化学的に相対的に貴な金属と卑な金属と
により1対の検出電極を形成し、この1対の検出電極を
相互に所定間隔だけ離して液体中に配置してガルバーニ
電池を形成し、この電池の前記1対の検出電極間を外部
回路により電気的に接続してこの電池系を閉回路電池系
となし、この閉回路電池系の電圧または電流を検出し、
この検出した電圧または電流から前記液体とこの液体中
の汚泥との界面の変化を検出する電極式汚泥界面計に関
する。DETAILED DESCRIPTION OF THE INVENTION According to the present invention, a pair of detection electrodes is formed from an electrochemically relatively noble metal and a base metal, and the pair of detection electrodes are separated from each other by a predetermined distance. A galvanic battery is formed by placing it in a liquid, and the pair of detection electrodes of this battery are electrically connected by an external circuit to make this battery system a closed circuit battery system, and the voltage of this closed circuit battery system is or detect current,
The present invention relates to an electrode type sludge interface meter that detects a change in the interface between the liquid and the sludge in the liquid from the detected voltage or current.
電極式汚泥界面計の原理構成図を第1図に示す。Figure 1 shows the basic configuration of the electrode type sludge interface meter.
’ この電極式汚泥界面計は特開昭50−71392号
により公知である。図において、カソード電極2は電気
化学的に相対的に貴な金属たとえばステンレス鋼よりな
る電極であり、アノード電極3は卑な金属たとえばタグ
タイル鋳鉄などの鉄よりな・ る電極であり、この両電
極2、3からなる電極系1を沈澱池4に浸漬する。そし
て、外部に負荷抵抗5を接続して閉回路を形成すると、
ステンレス電極2に溶存酸素の還元が生じ、タグタイル
鋳鉄電極3に鉄の溶解により水酸化鉄および酸化鉄がO
生成され、これらの電気化学的反応に対応じて、カソ
ード電極2、アノード電極3および負荷抵抗5よりなる
閉回路に電流路が形成され、負荷抵抗5に電圧降下が生
じる。ところで、この電圧は電極表面における有効酸”
5 素濃度に大きく依存する。'This electrode type sludge interface meter is known from Japanese Patent Laid-Open No. 71392/1983. In the figure, the cathode electrode 2 is an electrode made of an electrochemically relatively noble metal such as stainless steel, and the anode electrode 3 is an electrode made of a base metal such as iron such as tag tile cast iron. An electrode system 1 consisting of 2 and 3 is immersed in a sedimentation tank 4. Then, when a load resistor 5 is connected externally to form a closed circuit,
Dissolved oxygen is reduced in the stainless steel electrode 2, and iron hydroxide and iron oxide are dissolved in the tag tile cast iron electrode 3 due to dissolution of iron.
In response to these electrochemical reactions, a current path is formed in a closed circuit consisting of the cathode electrode 2, the anode electrode 3, and the load resistor 5, and a voltage drop occurs across the load resistor 5. By the way, this voltage is the effective acid on the electrode surface.
5. Highly dependent on elementary concentration.
すなわち、たとえば沈澱池4の水6中の溶存酸素濃度は
数一 より10−に達する。一方、汚泥T中では溶存酸
素がほとんど零となつている上に、両電極2,3に向け
ての酸素の補給速度も水中6に比較して遅いと考えられ
るから、この両電極2,3の表面の有効酸素濃度は実質
的に零となる。このために、負荷抵抗5に降下する電圧
は両電極2,3が水6中にあるときは0.3V以上とな
り、両電極2,3が汚泥7にあるときは0.1V以下と
なり、明確な差異が生ずる。従つて汚泥7が両電極2,
3を埋没したとき電圧の低下として検知され、この電圧
変化は変換回路8により増幅され計測器10にレベル指
示され、リレー9の接点作動によりシーケンス回路11
を経て、排泥バルブ12に排泥信号を供給し、汚泥7の
排出が行われる。That is, for example, the dissolved oxygen concentration in the water 6 of the sedimentation tank 4 reaches 10- from the number 1. On the other hand, dissolved oxygen in the sludge T is almost zero, and the rate of oxygen replenishment toward both electrodes 2 and 3 is also considered to be slower than in water 6. The effective oxygen concentration on the surface becomes substantially zero. For this reason, the voltage that drops across the load resistor 5 is 0.3 V or more when both electrodes 2 and 3 are in water 6, and is 0.1 V or less when both electrodes 2 and 3 are in sludge 7, and is clearly A significant difference arises. Therefore, the sludge 7 is connected to both electrodes 2,
3 is buried, it is detected as a voltage drop, and this voltage change is amplified by the conversion circuit 8 and the level is indicated to the measuring device 10, and the contact of the relay 9 is activated to send the sequence circuit 11.
A sludge signal is then supplied to the sludge valve 12, and the sludge 7 is discharged.
なお、13は排泥ポンプである。この排泥時にはかなり
の水流が生ずるから両電極2,3の表面に付着された汚
泥7は水流によつて除去される。しかしながら、長期間
に亘つて使用すると、両電極2,3の表面が汚泥7によ
り汚染されるので、両電極2,3が水6中に存在するに
もかかわらず発生電圧が低下して、正確な界面検出が得
られなくなるという欠点があつた。本発明は土述の点に
鑑み、従来技術の欠点である電極表面の汚染による発生
電圧の低下を防ぎ、界面検出精度を維持し得る取扱保守
が容易な電極式汚泥界面計を提供することを目的とする
。このような目的は、本発明によれば、冒頭で述べた種
類の電極式汚泥界面計において、1対の検出電極の表面
に付着した汚泥を除去する際には、外部回路を切換えて
、1対の検出電極に、貴な金属よりなる検出電極が負電
位となりかつ卑な金属よりなる検出電極が正電位となる
ような直流電圧を印加することにより達成される。この
ような本発明によれば、貴な金属よりなる検出電極が負
電位となりかつ卑な金属よりなる検出電極が正電位とな
るような直流電圧を1対の検出電極に印加することによ
り、両電極においては水素ガスおよび酸素ガスが発生し
、このガス発生によつて両電極の表面に付着した汚泥は
有効に除去される。In addition, 13 is a sludge pump. During this sludge removal, a considerable amount of water flow is generated, so that the sludge 7 adhering to the surfaces of both electrodes 2 and 3 is removed by the water flow. However, when used for a long period of time, the surfaces of both electrodes 2 and 3 become contaminated with sludge 7, so even though both electrodes 2 and 3 are present in water 6, the generated voltage decreases, making it difficult to accurately The disadvantage was that accurate interface detection could not be obtained. In view of the above-mentioned points, the present invention aims to provide an electrode-type sludge interface meter that is easy to handle and maintain, which can prevent the drop in generated voltage due to contamination of the electrode surface, which is a drawback of the conventional technology, and maintain interface detection accuracy. purpose. According to the present invention, in the electrode-type sludge interface meter of the type mentioned at the beginning, when removing sludge adhering to the surface of a pair of detection electrodes, the external circuit is switched. This is achieved by applying a DC voltage to the pair of detection electrodes such that the detection electrode made of a noble metal has a negative potential and the detection electrode made of a base metal has a positive potential. According to the present invention, a DC voltage is applied to a pair of detection electrodes such that the detection electrode made of a noble metal has a negative potential and the detection electrode made of a base metal has a positive potential. Hydrogen gas and oxygen gas are generated at the electrodes, and the sludge adhering to the surfaces of both electrodes is effectively removed by this gas generation.
外部回路の切換えは切換スイツチを設け、この切換スイ
ツチを操作することにより行なう。A changeover switch is provided and the external circuit is changed over by operating the changeover switch.
切換スイツチは手動操作もしくは制御装置による周期的
な操作でもよい。次に本発明の実施例を図面に基合き、
詳細に説明する。The changeover switch may be operated manually or periodically by a control device. Next, examples of the present invention are based on the drawings,
Explain in detail.
第2図は本発明の一実施例の概略構成図を示す。FIG. 2 shows a schematic configuration diagram of an embodiment of the present invention.
図において第1図と同一の機能を有する部分は同一の符
号が付されている。通常、両電極2,3から成る電極系
1はガルバニツクセル方式の電池系として動作し、測定
が行なわれる。一方、両電極2,3の表面に付着した汚
泥を除去しようとする際には、制御装置15からの信号
により切換スイツチ16を切換えると、定電圧電源部1
4によつて、タグタール鋳鉄製アノード電極3が正電位
、ステンレス鋼製カソード電極2が負電位となるような
極性の直流電流が供給される。この印加電流によつて、
両電極2,3は電解系として動作し、カソード電極2の
表面では溶存酸素の還元および水素ガスの発生反応が生
ずる。アノード電極3の表面では鉄の溶解反応および酸
素の発生反応が生ずる。このとき両電極2,3における
ガス発生によつて、両電極2,3の表面に付着した汚泥
は有効に除去される。本発明者の実1験によれば、例え
ば、懸濁物4%の濃度の汚泥7中へ両電極2,3が浸漬
された後、この両電極2,3を水6中へ静かに引上げて
、500μN々iの電流密度を有する上述の極性の直流
電流が定電圧電源部14によつて印加されると、電極2
,3に付着した汚泥は、約15分でうろこ状になり剥離
された。また、1000ttA/c!N2の電流密度で
は同様に電極2,3に付着した汚泥は、約5分で完全に
除去された。これに反し上述の電流が印加されないで自
然剥離によるとき、汚泥7が完全に除去されるためには
約1日を必要とした。従つて、沈澱池4の排泥周期を例
えば4時間毎とすれば、電極系1を電解系として、両電
極2,3の表面に付着した汚泥7を除去するために、動
作する時間は5分ないし15分程度で十分であるから、
残りの時間は電極系1を電池系として水6中と汚泥7中
との界面検出動作を経続することができる。In the figure, parts having the same functions as in FIG. 1 are designated by the same reference numerals. Normally, the electrode system 1 consisting of both electrodes 2 and 3 operates as a galvanic cell type battery system to perform measurements. On the other hand, when attempting to remove sludge adhering to the surfaces of both electrodes 2 and 3, when the changeover switch 16 is switched in response to a signal from the control device 15, the constant voltage power supply unit 1
4 supplies a direct current with a polarity such that the anode electrode 3 made of tagtar cast iron has a positive potential and the cathode electrode 2 made of stainless steel has a negative potential. With this applied current,
Both electrodes 2 and 3 operate as an electrolytic system, and on the surface of the cathode electrode 2, a reaction occurs to reduce dissolved oxygen and generate hydrogen gas. On the surface of the anode electrode 3, an iron dissolution reaction and an oxygen generation reaction occur. At this time, due to gas generation at both electrodes 2 and 3, the sludge adhering to the surfaces of both electrodes 2 and 3 is effectively removed. According to the inventor's experiment, for example, after both electrodes 2 and 3 are immersed in sludge 7 with a concentration of 4% suspended matter, both electrodes 2 and 3 are gently pulled up into water 6. When a DC current of the above polarity having a current density of 500 μNi is applied by the constant voltage power supply section 14, the electrode 2
The sludge adhering to , 3 became scaly and peeled off in about 15 minutes. Also, 1000ttA/c! Similarly, at the current density of N2, the sludge adhering to electrodes 2 and 3 was completely removed in about 5 minutes. On the other hand, when the above-mentioned electric current was not applied and natural peeling was performed, it took about one day for the sludge 7 to be completely removed. Therefore, if the sedimentation tank 4 is drained every 4 hours, the electrode system 1 will operate for 5 hours to remove the sludge 7 attached to the surfaces of the electrodes 2 and 3 as an electrolytic system. About 15 minutes is enough, so
During the remaining time, the interface detection operation between the water 6 and the sludge 7 can be continued using the electrode system 1 as a battery system.
このように電池系または電解系動作時間の選択は制御装
置15によつて切換え信号時間が決められる。なお、タ
グタール鋳鉄アノード電極3は通常の鉄製アノード電極
よりも表面に生ずる酸化鉄(錆)が剥離されやすく、汚
泥は酸化鉄と共に容易に除去されるので長期の使用に堪
える。In this way, the selection of the battery system or electrolytic system operating time is determined by the switching signal time by the control device 15. It should be noted that the tagtar cast iron anode electrode 3 can be used for a long time because iron oxide (rust) generated on the surface is easily peeled off and sludge is easily removed together with the iron oxide compared to a normal iron anode electrode.
以上に説明するように本発明によれば、力ソード電極に
正電位、アノード電極に負電位を与える極性の直流電圧
を、手動操作または制御装置の切換信号により両電極に
印加することによつて、両電極は電池系より電解系に切
換えられ、両電極表面に発生するガスの物理的作用によ
り表面に付着した汚泥が容易に剥離され、両電極表面の
汚染による発生電圧の低下を防ぎ、界面検出精度を長期
にわたり維持することができるから、取扱・保守の容易
な電極式汚泥界面計としてその効果は極めて大である。As explained above, according to the present invention, a polarity DC voltage that gives a positive potential to the power sword electrode and a negative potential to the anode electrode is applied to both electrodes by manual operation or a switching signal from the control device. , both electrodes are switched from a battery system to an electrolytic system, and the sludge adhering to the surface is easily peeled off by the physical action of the gas generated on the surfaces of both electrodes, preventing a drop in the generated voltage due to contamination on the surfaces of both electrodes, and reducing the interface Since detection accuracy can be maintained over a long period of time, it is extremely effective as an electrode-type sludge interface meter that is easy to handle and maintain.
【図面の簡単な説明】
第1図は電極式汚泥界面計の原理構成図、第2図は本発
明の一実施例の概略構成図である。
1:電極系、2:カソード電極、3:アノード電極、4
:沈澱池、5:負荷抵抗、6:水中、7:汚泥、8:変
換回路、9:リレ一、10:計測器、11:シーケンス
回路、12:排泥バルブ、13:排泥ポンプ、14:定
電圧電源部、15:制御装置、16:切換スイツチ。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a diagram showing the principle structure of an electrode type sludge interface meter, and FIG. 2 is a schematic diagram showing an embodiment of the present invention. 1: Electrode system, 2: Cathode electrode, 3: Anode electrode, 4
: Sedimentation tank, 5: Load resistance, 6: Underwater, 7: Sludge, 8: Conversion circuit, 9: Relay, 10: Measuring instrument, 11: Sequence circuit, 12: Sludge valve, 13: Sludge pump, 14 : Constant voltage power supply section, 15: Control device, 16: Changeover switch.
Claims (1)
1対の検出電極を形成し、この1対の検出電極を相互に
所定間隔だけ離して液体中に配置してガルバーニ電池を
形成し、この電池の前記1対の検出電極間を外部回路に
より電気的に接続してこの電池系を閉回路電池系となし
、この閉回路電池系の電圧または電流を検出し、この検
出した電圧または電流から前記液体とこの液体中の汚泥
との界面の変化を検出する汚泥界面計において、前記1
対の検出電極の表面に付着した汚泥を除去する際には、
前記外部回路を切換えて、前記1対の検出電極に、貴な
金属よりなる検出電極が負電位となりかつ卑な金属より
なる検出電極が正電位となるような直流電圧を印加する
ことを特徴とする電極式汚泥界面計。 2 特許請求の範囲第1項記載の界面計において、外部
回路に切換スイッチを設け、前記1対の検出電極の表面
に付着した汚泥を除去する際には、前記切換スイッチを
操作して定電圧源の直流出力電圧を1対の検出電極に印
加することを特徴とする電極式汚泥界面計。 3 特許請求の範囲第2項記載の界面計において、制御
装置を設け、前記1対の検出電極の表面に付着した汚泥
を除去する際には、前記制御装置の出力信号により切換
スイッチを周期的に操作して定電圧源の直流出力電圧を
周期的に1対の検出電極に印加することを特徴とする電
極式汚泥界面計。[Claims] 1. A pair of detection electrodes is formed from an electrochemically relatively noble metal and a base metal, and the pair of detection electrodes are placed in a liquid with a predetermined distance from each other. to form a galvanic battery, electrically connect between the pair of detection electrodes of this battery by an external circuit to make this battery system a closed circuit battery system, and detect the voltage or current of this closed circuit battery system. In the sludge interface meter that detects a change in the interface between the liquid and the sludge in the liquid from the detected voltage or current,
When removing sludge adhering to the surface of the pair of detection electrodes,
The external circuit is switched to apply a DC voltage to the pair of detection electrodes such that the detection electrode made of a noble metal has a negative potential and the detection electrode made of a base metal has a positive potential. Electrode type sludge interface meter. 2. In the interface meter according to claim 1, a changeover switch is provided in the external circuit, and when removing sludge adhering to the surfaces of the pair of detection electrodes, the changeover switch is operated to set a constant voltage. An electrode type sludge interface meter characterized in that a DC output voltage of a source is applied to a pair of detection electrodes. 3. In the interface meter according to claim 2, a control device is provided, and when removing sludge adhering to the surfaces of the pair of detection electrodes, the changeover switch is periodically activated by an output signal of the control device. 1. An electrode-type sludge interface meter which is operated to periodically apply a DC output voltage of a constant voltage source to a pair of detection electrodes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52014593A JPS5934964B2 (en) | 1977-02-15 | 1977-02-15 | Electrode type sludge interface meter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52014593A JPS5934964B2 (en) | 1977-02-15 | 1977-02-15 | Electrode type sludge interface meter |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS53100273A JPS53100273A (en) | 1978-09-01 |
JPS5934964B2 true JPS5934964B2 (en) | 1984-08-25 |
Family
ID=11865462
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP52014593A Expired JPS5934964B2 (en) | 1977-02-15 | 1977-02-15 | Electrode type sludge interface meter |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5934964B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06143156A (en) * | 1992-09-21 | 1994-05-24 | Muromoto Tekko Kk | Tool for mounting and demounting hose band and tool for demounting hose |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2841509B2 (en) * | 2019-12-16 | 2022-05-30 | Santana Ramirez Alberto Andres | Process for cleaning cathodic surfaces in voltaic cells |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS503660A (en) * | 1973-05-14 | 1975-01-16 | ||
JPS5071392A (en) * | 1973-10-25 | 1975-06-13 |
-
1977
- 1977-02-15 JP JP52014593A patent/JPS5934964B2/en not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS503660A (en) * | 1973-05-14 | 1975-01-16 | ||
JPS5071392A (en) * | 1973-10-25 | 1975-06-13 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06143156A (en) * | 1992-09-21 | 1994-05-24 | Muromoto Tekko Kk | Tool for mounting and demounting hose band and tool for demounting hose |
Also Published As
Publication number | Publication date |
---|---|
JPS53100273A (en) | 1978-09-01 |
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