JP2764125B2 - Electrolytic apparatus having electrode protection function and electrode protection method - Google Patents

Electrolytic apparatus having electrode protection function and electrode protection method

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Publication number
JP2764125B2
JP2764125B2 JP1069068A JP6906889A JP2764125B2 JP 2764125 B2 JP2764125 B2 JP 2764125B2 JP 1069068 A JP1069068 A JP 1069068A JP 6906889 A JP6906889 A JP 6906889A JP 2764125 B2 JP2764125 B2 JP 2764125B2
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Japan
Prior art keywords
anode
voltage
electrode
wire
electrode protection
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JP1069068A
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Japanese (ja)
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JPH02247394A (en
Inventor
孝之 島宗
義明 菅沼
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PERUMERETSUKU DENKYOKU KK
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PERUMERETSUKU DENKYOKU KK
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Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、不溶性金属陽極を使用し主として該電極基
材の破壊電圧以上の高電圧で行う電解操作における電圧
の過大な上昇を検出して前記不溶性金属陽極を保護する
ための装置及び方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial application field) The present invention detects an excessive rise in voltage in an electrolysis operation using an insoluble metal anode mainly at a high voltage higher than the breakdown voltage of the electrode substrate. An apparatus and method for protecting the insoluble metal anode.

(従来技術とその問題点) 高電圧を必要とする電解装置例えば電気透析装置では
その電解槽のエレメント数にもよるが、全体の槽電圧は
100〜200V程度である。又海水電解槽でも電流密度が10A
/dm2の場合極間距離1cmごとに約5Vの電圧を必要とし従
って極間距離が2cmであると10Vの電圧に達する。更に高
速めっきでは電流密度が100A/dm2以上となることがあり
この場合硫酸浴中での槽電圧が100Vをしばしば越えるこ
とになる。これらの電解に使用される不溶性金属陽極の
電極基材はチタン又はチタン合金であり、ハロゲンを含
まない浴中でのその破壊電圧は約100V、ハロゲンを含む
浴の場合の破壊電圧は10V程度である。
(Conventional technology and its problems) In an electrolyzer requiring a high voltage, for example, an electrodialyzer, the total cell voltage depends on the number of elements in the electrolyzer.
It is about 100-200V. Current density is 10A even in seawater electrolyzer
/ For dm 2 requires a voltage of about 5V per interelectrode distance 1cm Therefore interelectrode distance reaches a certain the 10V voltage at 2 cm. Further, in high-speed plating, the current density may be 100 A / dm 2 or more, and in this case, the cell voltage in the sulfuric acid bath often exceeds 100 V. The electrode substrate of the insoluble metal anode used for these electrolysis is titanium or a titanium alloy, and its breakdown voltage in a halogen-free bath is about 100 V, and the breakdown voltage in a halogen-containing bath is about 10 V. is there.

前記不溶性金属陽極が正常に機能している場合の陽極
の電位は1〜2Vであり電極物質や電極基材に問題が生ず
ることはない。しかしながら電極物質が消耗したり電極
が寿命に達した場合等には電極が不働態化を起こし電流
が流れにくくなる。この場合複数の槽を直列に接続した
電解装置では最も抵抗の大きい部分つまり前記不働態化
した陽極に全槽電圧のうちの殆どの電圧が掛かり、電流
が零になると全槽電圧が該不働態化した陽極に掛かるこ
とになる。該陽極に掛かる電圧が硫酸浴の場合で100V、
ハロゲン含有浴では種類により異なるが塩素では約10V
を越えると電極基材であるチタン又はチタン合金の活性
溶解を引き起こして電極基材として再度使用し得ない状
態になる。
When the insoluble metal anode is functioning normally, the potential of the anode is 1 to 2 V, and there is no problem with the electrode material or the electrode substrate. However, when the electrode material is consumed or when the electrode reaches the end of its life, the electrode is inactivated and the current hardly flows. In this case, in the electrolytic apparatus in which a plurality of cells are connected in series, most of the total cell voltage is applied to the portion having the highest resistance, that is, the passivated anode, and when the current becomes zero, the total cell voltage becomes the passive state. Will be hung on the converted anode. The voltage applied to the anode is 100 V in the case of a sulfuric acid bath,
Approximately 10 V for chlorine, depending on the type of halogen-containing bath
If the temperature exceeds the above, active dissolution of titanium or a titanium alloy as an electrode substrate is caused, and the electrode substrate cannot be used again as an electrode substrate.

該状態になることを防止するために槽電圧を検出し該
槽電圧の異常により電極基材への電圧集中を発見する方
法が採用されている。通常の電解では電流はほぼ一定値
に維持されるため、何等かの原因で電解槽の抵抗値が上
昇すると槽電圧が上昇するので該上昇を検出することに
より電解槽の異常を見出す方法である。しかし実際には
槽電圧は陽極の状態のみで決定されるのではなく、陰極
の過電圧を含む抵抗、電解液の抵抗及び槽全体の経時的
な電圧変化、及び例えば透析槽の場合には透析膜の抵抗
等多くの要素の結合された値として前記槽電圧は決定さ
れる。従って槽電圧を測定することにより、電解系全体
のある個所の異常を検出することはできるが、該異常が
必ずしも電極に起因するものではなく、逆に電極に異常
が生じても他の個所の異常により前記電極の異常が相殺
されて槽電圧の変動原因が判別できないという欠点があ
る。更に例えば塩素等のハロゲン元素を含む電解の場合
その破壊電圧は僅か10V程度であり、この程度の電圧は
透析槽では日常の変動幅の範囲に入ることがあり、変動
幅を厳密に、つまり小さくて規定すると僅かな電極状態
の変化により頻繁に電解が停止して能率低下を来し、又
変動幅をゆるやかに、つまり大きく規定すると電極基材
に損傷を与える陽極抵抗値の変化を十分に検出できず前
記基材を破壊してしまうという問題点がある。
In order to prevent such a state, a method of detecting a cell voltage and detecting a voltage concentration on an electrode substrate based on an abnormality of the cell voltage has been adopted. In normal electrolysis, the current is maintained at a substantially constant value, so if the resistance value of the electrolytic cell rises for some reason, the cell voltage rises, so this is a method of detecting an abnormality in the electrolytic cell by detecting the rise. . However, in practice, the cell voltage is not determined solely by the state of the anode. The cell voltage is determined as a combined value of many factors, such as the resistance of the cell. Therefore, by measuring the cell voltage, it is possible to detect an abnormality at a certain point in the entire electrolytic system, but the abnormality is not necessarily caused by the electrode. There is a disadvantage that the abnormality of the electrode is canceled by the abnormality and the cause of the fluctuation of the cell voltage cannot be determined. Further, for example, in the case of electrolysis containing a halogen element such as chlorine, the breakdown voltage is only about 10 V, and such a voltage may fall within the range of daily fluctuation in a dialysis tank. If specified, a slight change in the state of the electrode frequently stops the electrolysis, leading to a decrease in efficiency. There is a problem that the substrate cannot be destroyed.

又この槽電圧の変動を検出方法以外にも、陽極電位を
直接モニターする方法も提案されているが、該方法は硫
酸水銀や甘汞等の参照電極を用い、陽極表面にルギン管
を設置してこれらをブリッジ回路に接続して前記陽極電
位を測定するという通常の実験室的な手法を実用槽に応
用するものであり、精密な測定は可能であるが連続して
計測したりモニターすることはできないという欠点があ
る。
In addition to the method of detecting the fluctuation of the cell voltage, a method of directly monitoring the anode potential has also been proposed. In this method, a reference electrode such as mercury sulfate or calomel is used, and a lugine tube is installed on the anode surface. It is to apply the usual laboratory method of measuring the anode potential by connecting these to a bridge circuit to a practical tank, and it is possible to perform precise measurement, but to measure or monitor continuously. There is a drawback that you can not.

(発明の目的) 本発明は、全槽電圧を測定する代わりに、各陽極の電
位を測定することにより、該陽極の異常を迅速に検出で
きる装置及び方法を提供することを目的とする。
(Object of the Invention) It is an object of the present invention to provide an apparatus and a method capable of quickly detecting an abnormality of an anode by measuring the potential of each anode instead of measuring the whole cell voltage.

(問題点を解決するための手段) 本発明は、不溶性金属陽極の近傍に、該不溶性金属陽
極と絶縁して耐食性を有する導電性線材を設置し、前記
陽極と該線材間の電圧差を検出し、該電圧差が所定値以
上になった際に、前記陽極への通電を停止しあるいは通
電量を減少させることを特徴とする電極保護機能を有す
る電解装置及び該装置を使用する電極の保護方法であ
る。
(Means for Solving the Problems) According to the present invention, a conductive wire that is insulated from the insoluble metal anode and has corrosion resistance is installed near the insoluble metal anode, and a voltage difference between the anode and the wire is detected. When the voltage difference becomes equal to or more than a predetermined value, the power supply to the anode is stopped or the amount of power supply is reduced, and an electrolytic device having an electrode protection function and protection of an electrode using the device. Is the way.

以下本発明を詳細に説明する。 Hereinafter, the present invention will be described in detail.

本発明に係わる電極保護機能を有する電解装置及び電
極の保護方法は、全槽電圧を検出する代わりに個別の陽
極電位を測定することにより該陽極の異常を迅速かつ確
実に検出しようとするものである。
The electrolysis apparatus having an electrode protection function and the electrode protection method according to the present invention are intended to detect abnormalities of the anode quickly and surely by measuring individual anode potentials instead of detecting the entire cell voltage. is there.

電解装置における電圧分布は、不溶性金属陽極とその
近傍の電解液間に通常は電解反応に要する平衡電圧とそ
れに対する過電圧及び若干のオーム損分の電圧が掛か
り、その大きさは酸素発生を伴う場合は標準水素電極を
基準として1.5〜2.5Vである。ここで陽極の不働態化が
生ずると前記過電圧又はオーム損分の電圧が大きくな
り、液と電極間の電位差が大きくなる。該電位差は陽極
が正常又は正常に近い状態で作動している間は数mV〜1V
の変動であるが、陽極が不働態化してくると1Vを越える
差となってくる。
The voltage distribution in an electrolyzer is usually such that the equilibrium voltage required for the electrolytic reaction, the overvoltage and the voltage corresponding to a small ohmic loss are applied between the insoluble metal anode and the electrolyte in the vicinity, and the magnitude is accompanied by the generation of oxygen. Is 1.5 to 2.5 V based on a standard hydrogen electrode. Here, when the passivation of the anode occurs, the overvoltage or the voltage corresponding to the ohmic loss increases, and the potential difference between the liquid and the electrode increases. The potential difference is several mV to 1 V while the anode is operating in a normal or near normal state.
However, when the anode becomes inactive, the difference exceeds 1V.

本発明装置あるいは本発明方法により達成すべきこと
は、前記陽極の不働態化を捉えかつ該不働態化に起因す
る電圧集中による電極基材の破壊を防止することであ
り、該破壊はハロゲンを含む電解においても10Vを越え
る領域で発生することから、数Vの変動を捉え通電の停
止等の措置を講ずれば良いことになる。
What is to be achieved by the apparatus or the method of the present invention is to capture the passivation of the anode and prevent the electrode substrate from being destroyed due to voltage concentration caused by the passivation. Even in the electrolysis including the above, since the generation occurs in a region exceeding 10 V, it is sufficient to take a change of several V and take measures such as stopping the energization.

このような大きな電圧変化を捉えるには従来の参照電
極を使用する電位測定法によらなくとも、電解液と陽極
間の電位差を測定するだけで目的が達成できることを見
出し本発明に至ったものである。
In order to catch such a large voltage change, it was found that the object can be achieved only by measuring the potential difference between the electrolyte and the anode without using a conventional potential measurement method using a reference electrode, and the present invention has been achieved. is there.

本発明装置及び方法は電解槽の両極のうち陽極の保護
用に関し、該陽極としては通常チタン等の弁金属の基材
上に貴金属やその酸化物を含む電極物質を被覆したいわ
ゆる不溶性金属陽極が対象とされるが、被覆物質は特に
これらに限定されるものではない。
The device and the method of the present invention relate to the protection of the anode among the two electrodes of the electrolytic cell.As the anode, a so-called insoluble metal anode, which is usually coated on a base material of a valve metal such as titanium with an electrode material containing a noble metal or an oxide thereof. Although covered, the coating material is not particularly limited to these.

該陽極と電解液間の電位差を測定するための導電性線
材は耐食性を有する通常の導線であればよく、一般的に
は白金の細線が使用されるが勿論他の任意の導電性材料
を使用してもよい。この線材は陽極と絶縁状態で設置す
る必要があり、通常は該線材をテフロン(商品名)製等
の耐食性チューブで包み込んで電解液中に設置する。該
線材の先端と前記陽極間の距離は特に限定されないが、
近過ぎると検出する陽極部が限定され、又遠過ぎると電
解液自体による抵抗例えば気泡による抵抗等による変動
要因が生ずるため、通常は1〜10mm程度が適当である。
この距離は陽極表面と前記自体の間の距離であり、上述
の通り該線材が耐食性材料等で絶縁されていれば該材料
を陽極に接触させて固定してもよく、前記距離の変動を
防止するためにはこの設置手段が最適である。
The conductive wire for measuring the potential difference between the anode and the electrolytic solution may be a normal conductive wire having corrosion resistance. Generally, a fine platinum wire is used, but of course, any other conductive material is used. May be. This wire must be installed in an insulated state from the anode. Usually, the wire is wrapped in a corrosion-resistant tube made of Teflon (trade name) or the like and installed in an electrolytic solution. The distance between the tip of the wire and the anode is not particularly limited,
If the distance is too close, the anode part to be detected is limited, and if the distance is too far, a variation factor occurs due to the resistance of the electrolytic solution itself, for example, the resistance due to bubbles. Therefore, usually about 1 to 10 mm is appropriate.
This distance is the distance between the anode surface and the body itself. If the wire is insulated with a corrosion-resistant material or the like as described above, the material may be fixed by contacting the anode to prevent fluctuation of the distance. This installation means is the most suitable for this.

本発明装置及び方法は、食塩電解等の通常の電解槽あ
るいは脱塩用等の透析槽として使用される。複数の電解
槽に単一電源で電流を供給して電解を行う場合には複数
の各陽極ごとに前記線材を設置し各陽極単位で異常の発
生を検出することが好ましい。
The apparatus and method of the present invention are used as a normal electrolytic cell for salt electrolysis or the like or a dialysis tank for desalination or the like. When performing electrolysis by supplying current to a plurality of electrolytic cells with a single power supply, it is preferable to install the wire for each of a plurality of anodes and detect the occurrence of an abnormality in each anode.

前記電圧差を測定するには、一端が前記陽極に近接し
て設置された前記線材の他端を適宜槽外に引き出し、電
圧計やブリッジ回路等により前記陽極と電位差を計測す
る。電解液の種類特にハロゲンを含む電解液か否かにも
よるが、該計測値が正常値より数V程度高くなった時点
で電源を切って電流を遮断するかあるいは電流量を減少
させて異常の生じた陽極へ掛かる電圧値を零にするか大
きく減少させて該陽極の損傷や破損を防止する。なお自
動的に電源の制御を行うのではなく異常が検出された際
に警告音を発して手動で電源の制御を行うようにしても
よい。
In order to measure the voltage difference, the other end of the wire, one end of which is placed close to the anode, is appropriately pulled out of the tank, and a potential difference from the anode is measured by a voltmeter, a bridge circuit, or the like. Depending on the type of electrolyte, particularly the electrolyte containing halogen, when the measured value is several volts higher than the normal value, the power is turned off and the current is cut off, or the amount of current is reduced to abnormally. The voltage applied to the anode where the cracks occur is reduced to zero or greatly reduced to prevent damage or breakage of the anode. Instead of automatically controlling the power supply, a warning sound may be emitted when an abnormality is detected, and the power supply may be controlled manually.

本発明装置あるいは方法により各陽極ごとの電位差を
計測するとともに全槽電圧の変動を検出すると、前記陽
極の異常だけでなく、電解槽の他の部位の異常も同時に
発見することができるので好都合である。
When the potential difference of each anode is measured by the apparatus or method of the present invention and the fluctuation of the whole cell voltage is detected, not only the abnormality of the anode but also the abnormality of other parts of the electrolytic cell can be simultaneously detected, which is convenient. is there.

(実施例) 以下本発明装置を実施例により説明するが該実施例は
本発明を限定するものではない。
(Examples) Hereinafter, the present invention will be described with reference to examples, but the examples do not limit the present invention.

実施例1 70槽の単位槽を有する電気透析槽のそれぞれの単位槽
に陽イオン交換膜と陰イオン交換膜を設置し、陽極とし
て板状チタン基材表面に酸化イリジウムを被覆した不溶
性金属陽極を又陰極としてニッケル板を使用し、電解液
として10%硫酸を満たして電気透析を行った。液電圧検
出用線材として直径0.2mmの白金線をテフロン製チュー
ブに挿入した。該白金線の先端には検出部を残して更に
テフロンチューブを巻きつけ外径が2mmとなるようにし
て陽極に貼り付けた。
Example 1 A cation exchange membrane and an anion exchange membrane were installed in each unit tank of an electrodialysis tank having 70 unit tanks, and an insoluble metal anode coated with iridium oxide on the surface of a plate-like titanium substrate was used as an anode. Electrodialysis was performed using a nickel plate as a cathode and 10% sulfuric acid as an electrolyte. A 0.2 mm diameter platinum wire was inserted into a Teflon tube as a liquid voltage detection wire. A Teflon tube was further wound around the tip of the platinum wire, leaving a detection unit, and attached to the anode so that the outer diameter became 2 mm.

該白金線と陽極間の電圧差を計測するために電圧制御
装置を備えた電圧計を設置し、前記白金線をマイナス側
に陽極をプラス側に接続した。前記電気透析槽の陽極の
正常時の電圧が2Vで±0.5V程度の変動が予想されたため
制御電圧を5Vにセットし、5Vを越えると赤ランプが点灯
するとともに電源が切れるようにした。
A voltmeter equipped with a voltage controller was installed to measure the voltage difference between the platinum wire and the anode, and the platinum wire was connected to the minus side and the anode was connected to the plus side. Since the normal voltage of the anode of the electrodialysis tank was 2 V and a fluctuation of about ± 0.5 V was expected, the control voltage was set to 5 V. When the voltage exceeded 5 V, the red lamp was turned on and the power was turned off.

加速条件で2000時間運転後、正常条件で運転を継続し
た。全槽電圧は135Vであった。そのまま正常運転を継続
したところ1300時間運転後に赤ランプが点灯し電源が切
れた。陽極のチェックを行ったところ、陽極電位は部分
的に3Vを越えており、寿命が切れたものと判定された。
陽極基材自体には異常は観察されなかった。
After operating for 2000 hours under acceleration conditions, operation was continued under normal conditions. The total cell voltage was 135V. When normal operation was continued, the red lamp turned on and the power was turned off after 1300 hours of operation. When the anode was checked, the anode potential partially exceeded 3 V, and it was determined that the life was expired.
No abnormality was observed on the anode substrate itself.

実施例2 単位槽の数を30槽とし、電解液を3%食塩水とし、液
検出用線材を陽極から5mm離間させたこと以外は実施例
1と同様にして前記食塩水の淡水化を行った。制御電位
は3Vにセットし、陽極電流密度を2A/dm2となるようにし
た。
Example 2 Desalination of the saline was carried out in the same manner as in Example 1 except that the number of unit cells was 30, the electrolyte was 3% saline, and the wire for liquid detection was separated from the anode by 5 mm. Was. The control potential was set to 3 V, and the anode current density was set to 2 A / dm 2 .

この条件で電解を継続したところ、全槽電圧は電解の
進行状況に応じて60〜75Vの範囲内で変動し、電圧計は
1.8Vを示していた。
When electrolysis was continued under these conditions, the total cell voltage fluctuated within the range of 60 to 75 V depending on the progress of electrolysis, and the voltmeter
1.8V was shown.

約3000時間運転後、電圧計の指針が徐々に上昇し始め
3Vに達して電源が停止した。前記陽極を取り出したとこ
ろ、外観上の変化はみられ無かったがコーティングの電
位が1V上昇しており、該陽極は寿命に達していることが
分かった。
After approximately 3000 hours of operation, the voltmeter pointer begins to gradually rise
The power supply stopped after reaching 3V. When the anode was taken out, there was no change in appearance, but the potential of the coating increased by 1 V, indicating that the anode had reached the end of its life.

比較例 液検出用線材を設置しなかったこと以外は実施例2と
同一の電解槽を準備し、実施例2と同一条件で食塩の淡
水化を行った。
Comparative Example The same electrolytic cell as in Example 2 was prepared except that the wire for liquid detection was not installed, and salt water was desalinated under the same conditions as in Example 2.

約3000時間運転後、全槽電圧が85Vに上昇して電流値
が半分に低下し、しばらくすると白色の液が陽極室から
流れだした。電源を切って槽を分解したところ、陽極表
面のコーティングは全て消失し、陽極基材は腐食してぼ
ろぼろになっており再使用が不能であった。
After about 3000 hours of operation, the total cell voltage increased to 85 V, the current value decreased by half, and after a while, a white liquid began to flow from the anode chamber. When the power was turned off and the tank was disassembled, the coating on the anode surface was completely lost, and the anode substrate was corroded and ragged, and could not be reused.

(発明の効果) 本発明に係わる電極保護機能を有する電解装置及び電
極保護方法は、不溶性金属陽極を使用して特に高電圧下
で電解を行うに際し、従来のように全槽電圧の変動を検
出するのではなく、各陽極と電解液間の電位差を計測し
て異常を検出するようにしている。
(Effect of the Invention) The electrolysis apparatus having an electrode protection function and the electrode protection method according to the present invention detects the fluctuation of the whole cell voltage as in the related art when performing electrolysis using an insoluble metal anode, particularly under a high voltage. Instead, the potential difference between each anode and the electrolyte is measured to detect an abnormality.

従って従来のように陰極や隔膜のような他の要因によ
る影響を受けることなく、陽極の状態にのみにより決定
される陽極電位を計測することにより、該陽極の異常を
迅速かつ確実に検出することが可能になる。該検出に基
づき電源を停止する等の適宜の対応により前記陽極の損
傷や破損を確実に防止することができる。
Therefore, by measuring the anode potential determined only by the state of the anode without being affected by other factors such as the cathode and the diaphragm as in the related art, the abnormality of the anode can be detected quickly and reliably. Becomes possible. By taking appropriate measures such as stopping the power supply based on the detection, damage or breakage of the anode can be reliably prevented.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】不溶性金属陽極、該不溶性金属陽極の近傍
に該不溶性金属陽極と絶縁して設置された耐食性を有す
る導電性線材、前記陽極と該線材間の電圧差を検出する
電圧検出計とを含んで成り、該電圧検出計により検出さ
れた前記電圧差が所定値以上になった際に、前記陽極へ
の通電を停止しあるいは通電量を減少させることを特徴
とする電極保護機能を有する電解装置。
1. An insoluble metal anode, a conductive wire having corrosion resistance installed in the vicinity of the insoluble metal anode and insulated from the insoluble metal anode, a voltage detector for detecting a voltage difference between the anode and the wire. When the voltage difference detected by the voltage detector becomes equal to or more than a predetermined value, the electrode has a function of protecting the anode by stopping or reducing the amount of electricity to the anode. Electrolysis equipment.
【請求項2】不溶性金属陽極の近傍に、該不溶性金属陽
極と絶縁して耐食性を有する導電性線材を設置し、前記
陽極と該線材間の電圧差を検出して該電圧差が所定値以
上になった際に、前記陽極への通電を停止しあるいは通
電量を減少させることを特徴とする電解装置の電極保護
方法。
2. A conductive wire, which is insulated from the insoluble metal anode and has corrosion resistance, is installed near the insoluble metal anode, and a voltage difference between the anode and the wire is detected and the voltage difference is equal to or more than a predetermined value. A method for protecting an electrode of an electrolysis apparatus, comprising:
JP1069068A 1989-03-20 1989-03-20 Electrolytic apparatus having electrode protection function and electrode protection method Expired - Lifetime JP2764125B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1069068A JP2764125B2 (en) 1989-03-20 1989-03-20 Electrolytic apparatus having electrode protection function and electrode protection method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1069068A JP2764125B2 (en) 1989-03-20 1989-03-20 Electrolytic apparatus having electrode protection function and electrode protection method

Publications (2)

Publication Number Publication Date
JPH02247394A JPH02247394A (en) 1990-10-03
JP2764125B2 true JP2764125B2 (en) 1998-06-11

Family

ID=13391889

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1069068A Expired - Lifetime JP2764125B2 (en) 1989-03-20 1989-03-20 Electrolytic apparatus having electrode protection function and electrode protection method

Country Status (1)

Country Link
JP (1) JP2764125B2 (en)

Also Published As

Publication number Publication date
JPH02247394A (en) 1990-10-03

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