JP2002275663A - Electrolytic protection process - Google Patents

Electrolytic protection process

Info

Publication number
JP2002275663A
JP2002275663A JP2001080244A JP2001080244A JP2002275663A JP 2002275663 A JP2002275663 A JP 2002275663A JP 2001080244 A JP2001080244 A JP 2001080244A JP 2001080244 A JP2001080244 A JP 2001080244A JP 2002275663 A JP2002275663 A JP 2002275663A
Authority
JP
Japan
Prior art keywords
electrode
protection
anticorrosion
cathodic protection
protected
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.)
Withdrawn
Application number
JP2001080244A
Other languages
Japanese (ja)
Inventor
Yuusuke Ichinose
祐亮 一ノ瀬
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2001080244A priority Critical patent/JP2002275663A/en
Publication of JP2002275663A publication Critical patent/JP2002275663A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a process for electrolytic protection in the atmosphere for secure electrolytic protection of a coated surface. SOLUTION: In the process, a coating is applied to the metallic surface of a protection target, an electrode for electrolytic protection is established as a positive pole on the coated surface via an insulator, and an electric current is applied using the protection target as a negative pole to perform electrolytic protection of the protection target. Here, the electric current generated by a generator attached to a movable part of the protection target is rectified and applied to the electrode and the protection target.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は大気中の電気防食方
法に関し、特にベルトコンベアーの架台の電気防食に適
する方法に係る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for preventing cathodic corrosion in the atmosphere, and more particularly to a method suitable for cathodic protection of a gantry of a belt conveyor.

【0002】[0002]

【従来の技術】大気中の電気防食システムの概要を、図
4に示す。防食対象物3は、金属表面を塗装し、塗膜4
上に絶縁物7を介して電気防食用電極1を正極、防食対
象物3を負極として電源2とを導線5により結線する。
金属表面が乾燥し、液膜が形成されない状態では防食電
流が流れないが、乾燥状態では錆の発生がないために防
食の必要性がない。降雨等により塗装表面が濡れ、液膜
6が形成された場合に錆が進展するが、液膜6を媒体と
して電気が流れると塗膜欠陥の錆の進展が防止されて塗
膜の寿命が格段に長くなる。
2. Description of the Related Art An outline of an atmospheric cathodic protection system is shown in FIG. The anticorrosion target 3 is formed by coating a metal surface and applying a coating 4
The electrode 1 for cathodic protection is used as a positive electrode and the object 3 to be used as a negative electrode via an insulator 7, and the power supply 2 is connected to the power supply 2 with a conducting wire 5.
In a state where the metal surface is dried and a liquid film is not formed, no anticorrosion current flows, but there is no need for anticorrosion in a dry state since no rust is generated. Rust develops when the coating surface is wet due to rainfall or the like and the liquid film 6 is formed, but when electricity flows using the liquid film 6 as a medium, the rust of coating film defects is prevented from developing and the life of the coating film is significantly improved. Become longer.

【0003】しかし、図3に示すようなベルトコンベア
ーは長さが数百メートル以上にもなり、モータ15まで
しか商用電源がない場合があり、架台16すべてを電気
防食するには架台16にそって数百mも導線5を配線す
る必要があり、設置のためのコストが大幅に増加する。
導線5が長くなると、導線5が途中で切れることも多く
なり防食効果を維持することが困難になる。
However, a belt conveyor as shown in FIG. 3 has a length of several hundred meters or more, and there is a case where only a motor 15 has a commercial power supply. Therefore, it is necessary to wire the conducting wire 5 for several hundred meters, which greatly increases the cost for installation.
When the length of the conductive wire 5 is long, the conductive wire 5 is often cut in the middle, and it is difficult to maintain the anticorrosion effect.

【0004】また、架台に沿ってすでに配線されている
場合も、流れている電流が高電圧の交流であることが多
く、電気防食用に必要とされる1〜20V程度の直流に
変換するための分電工事、電圧を下げる装置及び直流化
する装置の設置工事が必要となり、分電工事時には流れ
ている電気をOFFにする必要があり、常時稼働してい
る設備においては工事そのものが不可能であったり、電
気防食が必要な各部にこのような工事をすると設置コス
トが増加する。防食対象物に供給している電気容量に余
裕がない場合には装置全体の電気容量を増やすための工
事も必要となり更に設置コストが増加する。
[0004] In addition, even when already wired along the frame, the current flowing is often a high-voltage alternating current, and is converted to a direct current of about 1 to 20 V required for cathodic protection. Power distribution work, installation of equipment to reduce voltage and installation of direct current conversion equipment are required, and it is necessary to turn off the electricity flowing at the time of power distribution work, and the construction itself is not possible with equipment that is constantly operating In addition, if such a construction is performed on each part that requires cathodic protection, the installation cost increases. If the electric capacity supplied to the anticorrosion target has no margin, construction for increasing the electric capacity of the entire apparatus is also required, and the installation cost further increases.

【0005】このような課題を解決する方法として、図
5に示すように、電源として太陽電池2′と犠牲電極
1′を組合せた発明が開示されている(特開平7−31
6850号公報)。この発明は、太陽が照射されている
状態では太陽電池2′により発電された電気により防食
し、太陽が照射されない夜間や雨天時には切りかえスイ
ッチ13により電源部を切りかえて犠牲電極1′の溶解
により発生した電気により防食する方法である。本方法
は、商用電源から遠く離れた防食対象物16においても
長い導線5が必要なく防食が可能である。
As a method for solving such a problem, as shown in FIG. 5, an invention in which a solar cell 2 'and a sacrificial electrode 1' are combined as a power source is disclosed (Japanese Patent Laid-Open No. 7-31).
No. 6850). According to the present invention, when the sun is irradiated, corrosion is prevented by the electricity generated by the solar cell 2 ', and at night or when the sun is not irradiated, the power switch is switched by the switch 13 to dissolve the sacrificial electrode 1'. This is a method of preventing corrosion by using electricity. According to the present method, anticorrosion can be performed on the anticorrosion target 16 far from the commercial power supply without the need for the long conductive wire 5.

【0006】しかし、大気中の電気防食は、太陽の照射
量が少ない雨天時の雨や夜間に結露する水により腐食が
進行するため、太陽電池2′により発生する電気は有効
に使用されず、犠牲電極1′の溶損により発生する電流
の方が防食に大きく寄与し、犠牲電極1′の寿命が本シ
ステムの寿命となる。また、水中や土中の防食対象物と
異なり、大気中の対象物16の表面に形成される液膜6
の抵抗は高いため、水中や土中の電気防食で適用されて
る犠牲電極1′により発生する電気では電圧が低すぎて
防食範囲が狭くなり、犠牲電極1′を多く設置する必要
が生じてコストが増加する。また、雨天や夜間時でも十
分な電位を確保するために太陽電池2′のパネルを大き
くしてもコストが増加し、そのパネルの固定方法も困難
となる。
[0006] However, in the cathodic protection in the atmosphere, since the corrosion proceeds due to rain in rainy weather when the amount of sun irradiation is small or water condensed at night, electricity generated by the solar cell 2 'is not used effectively. The current generated by the erosion of the sacrificial electrode 1 'greatly contributes to corrosion prevention, and the life of the sacrificial electrode 1' is the life of the present system. Further, unlike the anticorrosion target in water or soil, the liquid film 6 formed on the surface of the target 16 in the atmosphere
Is high, the voltage generated by the sacrificial electrode 1 'applied in water and in the soil to protect the sacrificial electrode 1' is too low to narrow the anticorrosion range. Increase. Further, even if the panel of the solar cell 2 'is enlarged in order to secure a sufficient potential even in rainy weather or at night, the cost increases, and the method of fixing the panel becomes difficult.

【0007】[0007]

【発明が解決しようとする課題】前記従来の技術は、電
源から遠い大気中の防食対象物へ電気防食をするには設
置コストが距離に比例して増加するという問題点があっ
た。そこで本発明は、商用電源が無くとも防食が可能な
大気中の電気防食の方法を提供することを目的とする。
However, the conventional technique has a problem that the cost of installation increases in proportion to the distance in order to carry out the electrolytic protection of an object to be protected in the atmosphere far from the power supply. Accordingly, an object of the present invention is to provide a method of cathodic protection in the atmosphere that can be protected without a commercial power supply.

【0008】[0008]

【課題を解決するための手段】本発明の電気防食方法以
下の通りである。 (1)防食対象物の金属表面を塗装し、塗装表面上に絶
縁物を介して電気防食用電極を正極として設置し、防食
対象物を負極として電気を流し、防食対象物の電気防食
をする方法において、防食対象物の運動部に取付けられ
た発電器から発生した電流を整流して前記電極及び前記
防食対象物に通電することを特徴とする電気防食方法、 (2)発電器から発生した電流を整流し充電池に充電し
た後、前記充電池と前記電極及び前記防食対象物に通電
することを特徴とする(1)記載の電気防食方法であ
る。
The cathodic protection method of the present invention is as follows. (1) Paint the metal surface of the anticorrosion target, place an electrode for cathodic protection as a positive electrode via an insulator on the coating surface, and conduct electricity using the anticorrosion target as a negative electrode to perform anticorrosion of the anticorrosion target. A method of rectifying a current generated from a generator attached to a moving part of the object to be eroded and energizing the electrode and the object to be protected, (2) generated from the generator The method according to (1), wherein after the current is rectified and the rechargeable battery is charged, the rechargeable battery, the electrode, and the anticorrosion target are energized.

【0009】[0009]

【発明の実施の形態】以下に、本発明を詳細に説明す
る。図1に示すように、運動部11に回転体8を接触さ
せ、運動体11の動きを回転運動に変換して発電器9を
回して発電する。回転体8は運動部の動力源であるモー
ターを利用しても良いし、モーターとは別個に設けても
良い。発電器9により発電された電気は交流であるた
め、整流器10にて直流に変換し、電気防食用電極1を
正極、防食対象物3を負極として導線5で結線する。防
食対象物3の表面は塗装を行い、そのうえに絶縁物7を
介して電極1を装着する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. As shown in FIG. 1, the rotating body 8 is brought into contact with the moving unit 11, the movement of the moving body 11 is converted into a rotational movement, and the generator 9 is turned to generate power. The rotating body 8 may use a motor that is a power source of the moving unit, or may be provided separately from the motor. Since the electricity generated by the generator 9 is an alternating current, it is converted to a direct current by the rectifier 10 and connected by the conducting wire 5 with the electrode 1 for the cathodic protection and the object 3 to be corroded as the negative electrode. The surface of the anticorrosion target 3 is coated, and the electrode 1 is mounted thereon via an insulator 7.

【0010】防食対象物の材質は電気防食のしやすさと
適用が多いため、鉄鋼材料であることが好ましい。塗膜
の材料は、フェノール樹脂、アクリル樹脂、エポキシ樹
脂、ポリウレタン樹脂等を使用できる。電気防食用電極
はアルミニウム、チタン等を使用できる。絶縁物はゴ
ム、樹脂、セラミックス等を使用できる。
The material of the anticorrosion target is preferably an iron or steel material because of its easiness of electrocorrosion protection and its many applications. As a material of the coating film, a phenol resin, an acrylic resin, an epoxy resin, a polyurethane resin, or the like can be used. Aluminum, titanium or the like can be used for the electrode for cathodic protection. As the insulator, rubber, resin, ceramics, or the like can be used.

【0011】運動部11が常時運動するような設備であ
れば、整流器10から発生する直流電流を直接、電気防
食用電極1、防食対象物3に接続して安定した防食電圧
を維持することが可能であるが、運動体11が動いたり
止まったりするような設備の場合は、整流後の電流を蓄
電池12に充電し、設備が動かない時は蓄電池12の電
気により電気防食を行うことにより安定した大気中の電
気防食が可能である。
If the moving unit 11 is a facility that constantly moves, the direct current generated from the rectifier 10 can be directly connected to the electrode 1 and the object 3 to maintain a stable corrosion protection voltage. It is possible, but in the case of equipment in which the moving body 11 moves or stops, the storage battery 12 is charged with the rectified current, and when the equipment does not move, it is stabilized by performing cathodic protection by the electricity of the storage battery 12. It is possible to prevent cathodic corrosion in the atmosphere.

【0012】防食対象物の表面に形成される液膜の電気
伝導度により設定電圧は異なり、通常の大気中環境に設
置され表面を塗装した防食対象物の場合は、1〜20V
の範囲とすることが好ましい。防食対象物の表面に形成
される液膜の抵抗が低いときに高い電圧を設定すると、
電流が流れすぎて電極の周りで過防食となり塗膜の剥離
が発生し、塗膜寿命を逆に短くしてしまう。一方、液膜
の抵抗が高いときに、低い電圧に設定すると、電流が流
れる防食範囲が狭くなり、防食対象物全体を防食するに
は、多くの電極を設置する必要があり、設置コストが高
くなる。
The set voltage differs depending on the electric conductivity of the liquid film formed on the surface of the anticorrosion target. In the case of the anticorrosion target which is installed in a normal atmospheric environment and whose surface is coated, 1 to 20 V is applied.
It is preferable to set it in the range. If a high voltage is set when the resistance of the liquid film formed on the surface of the anticorrosion target is low,
When the current flows too much, it becomes over-corrosion-proof around the electrode, and peeling of the coating film occurs, thereby shortening the life of the coating film. On the other hand, when the resistance of the liquid film is high, if the voltage is set to a low voltage, the anticorrosion range in which the current flows becomes narrow, and in order to prevent the entire anticorrosion target from being corroded, it is necessary to install many electrodes, and the installation cost is high. Become.

【0013】整流器に配線する電気防食用電極は1個で
ある必要はなく、2個以上の電極の設置も可能である。
配線する電気防食用電極の数を増やすと発電器、整流器
の個数を減らすことになるが、電気防食用電極と整流器
間の配線の距離が長くなるため、防食対象設備ごとに、
設定電圧、電極の配線を決定すればよい。
[0013] The number of electrodes for the cathodic protection to be wired to the rectifier need not be one, and two or more electrodes can be provided.
Increasing the number of cathodic protection electrodes to be wired will reduce the number of generators and rectifiers, but the distance between the cathodic protection electrodes and the rectifiers will be longer, so for each equipment subject to corrosion protection,
The set voltage and electrode wiring may be determined.

【0014】[0014]

【実施例】実施例として、ベルトコンベアーを防食した
場合を図1から図3に示す。ベルトコンベアーの鋼製架
台16の表面は塗装され、塗膜4上に絶縁物7を介して
電気防食用電極1を設置する。塗膜の組成はエポキシ樹
脂であり、絶縁物としてゴムを使用し、電気防食用電極
の材質はアルミニウムとした。架台上に設置している支
持ロール17に直結した発電器9により、交流が発生
し、整流器10により直流に変換される。変換された直
流電流は、電気防食用電極を正極、防食対象物である架
台16を負極として導線5により結線し、電圧を付加す
ることにより防食する。支持ロール17を回転体8とす
ることにより、移動運動を回転運動に確実に変換できて
装置も簡略化する。設定電圧は10Vとした。整流器に
配線する電気防食用電極1は6個とした。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIGS. 1 to 3 show an embodiment in which a belt conveyor is protected from corrosion. The surface of the steel base 16 of the belt conveyor is painted, and the electrode 1 for cathodic protection is installed on the coating film 4 via the insulator 7. The composition of the coating film was an epoxy resin, rubber was used as an insulator, and the material of the electrode for cathodic protection was aluminum. An alternating current is generated by a power generator 9 directly connected to a support roll 17 installed on a gantry, and is converted to a direct current by a rectifier 10. The converted DC current is connected by the conductive wire 5 with the electrode for cathodic protection as the positive electrode and the gantry 16 as the anticorrosion target as the negative electrode, and is protected by applying a voltage. By using the supporting roll 17 as the rotating body 8, the moving motion can be reliably converted to the rotating motion, and the apparatus can be simplified. The set voltage was 10 V. The number of the electrodes for cathodic protection to be wired to the rectifier was six.

【0015】[0015]

【発明の効果】防食対象物の運動体から発電された電気
を、電気防食の電源として用いることにより、商用電源
からの距離が遠い設備に対しても、安価に安定した防食
が可能となる。また、蓄電池を組合せることにより、運
動体の運動が、動いたり止まったりする設備に対しても
安定した防食が可能となる。
As described above, by using the electricity generated from the moving object of the anticorrosion target as a power source for the anticorrosion, stable and low-cost anticorrosion can be achieved even for equipment far from the commercial power supply. In addition, by combining the storage batteries, stable corrosion prevention can be performed even on equipment in which the movement of the moving body moves or stops.

【図面の簡単な説明】[Brief description of the drawings]

【図1】発電器を用いた本発明の概略を示す図である。FIG. 1 is a diagram showing an outline of the present invention using a power generator.

【図2】発電器と蓄電器を用いた本発明の概略を示す図
である。
FIG. 2 is a diagram showing an outline of the present invention using a power generator and a storage battery.

【図3】本発明を適用したベルトコンベアーの側面図で
ある。
FIG. 3 is a side view of a belt conveyor to which the present invention is applied.

【図4】従来の大気中電気防食方法の概略を示す図であ
る。
FIG. 4 is a view schematically showing a conventional atmospheric cathodic protection method.

【図5】太陽電池と犠牲電極を組合せた従来の大気中電
気防食方法の概略を示す図である。
FIG. 5 is a view schematically showing a conventional atmospheric anticorrosion method combining a solar cell and a sacrificial electrode.

【符号の説明】[Explanation of symbols]

1 :電気防食用電極 1′:犠牲電極 2 :直流電源 2′:太陽電池 3 :防食対象物 4 :塗膜 5 :導線 6 :液膜 7 :絶縁物 8 :回転体 9 :発電器 10:整流器 11:運動部 12:充電池 13:切りかえスイッチ 14:ベルト 15:モータ 16:架台 17:支持ロール 1: Electrode for corrosion protection 1 ': Sacrificial electrode 2: DC power supply 2': Solar cell 3: Corrosion protection object 4: Coating film 5: Conductive wire 6: Liquid film 7: Insulator 8: Rotating body 9: Generator 10: Rectifier 11: Moving part 12: Rechargeable battery 13: Switching switch 14: Belt 15: Motor 16: Stand 17: Support roll

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 防食対象物の金属表面を塗装し、塗装表
面上に絶縁物を介して電気防食用電極を正極として設置
し、防食対象物を負極として電気を流し、防食対象物の
電気防食をする方法において、防食対象物の運動部に取
付けられた発電器から発生した電流を整流して前記電極
及び前記防食対象物に通電することを特徴とする電気防
食方法。
1. A metal surface of an object to be protected is coated, an electrode for cathodic protection is installed as a positive electrode via an insulator on the surface of the coating, and electricity is passed using the object to be protected as a negative electrode. The method according to claim 1, wherein a current generated from a generator attached to a moving part of the object to be protected is rectified to supply current to the electrode and the object to be protected.
【請求項2】 発電器から発生した電流を整流し充電池
に充電した後、前記充電池と前記電極及び前記防食対象
物に通電することを特徴とする請求項1記載の電気防食
方法。
2. The method according to claim 1, wherein after rectifying the current generated from the generator and charging the rechargeable battery, the rechargeable battery, the electrode and the object to be protected are energized.
JP2001080244A 2001-03-21 2001-03-21 Electrolytic protection process Withdrawn JP2002275663A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001080244A JP2002275663A (en) 2001-03-21 2001-03-21 Electrolytic protection process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001080244A JP2002275663A (en) 2001-03-21 2001-03-21 Electrolytic protection process

Publications (1)

Publication Number Publication Date
JP2002275663A true JP2002275663A (en) 2002-09-25

Family

ID=18936558

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001080244A Withdrawn JP2002275663A (en) 2001-03-21 2001-03-21 Electrolytic protection process

Country Status (1)

Country Link
JP (1) JP2002275663A (en)

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