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JP7066465B2 - Method for forming anticorrosion electrodeposition coating on underwater metal structures - Google Patents
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JP7066465B2 - Method for forming anticorrosion electrodeposition coating on underwater metal structures - Google Patents

Method for forming anticorrosion electrodeposition coating on underwater metal structures Download PDF

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JP7066465B2
JP7066465B2 JP2018051880A JP2018051880A JP7066465B2 JP 7066465 B2 JP7066465 B2 JP 7066465B2 JP 2018051880 A JP2018051880 A JP 2018051880A JP 2018051880 A JP2018051880 A JP 2018051880A JP 7066465 B2 JP7066465 B2 JP 7066465B2
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達志 岩本
靖庸 鈴木
晴喜 谷口
浩一朗 山田
圭介 田村
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Description

本開示は、水中金属構造物の防食電着被膜形成方法に関するものである。 The present disclosure relates to a method for forming an anticorrosion electrodeposition film on an underwater metal structure.

一般に、水中金属構造物としては、岸壁等に護岸のために設けられる鋼矢板、橋梁や桟橋等に設けられる鋼管杭、或いはコンクリート構造物の表面を鉄鋼部材で被覆した鋼ケーソン等の海洋鋼構造物が含まれている。前記水中金属構造物は、海中への水没と大気露出が繰り返される、いわゆる干満帯、並びに干満にかかわらず常時水没している水中部において、海水或いは汽水(淡水と海水が混在した状態の液体)に接触する状態で設けられており、非常に錆が発生し易い環境に晒されている。 Generally, as an underwater metal structure, a steel sheet pile provided for berthing on a quay or the like, a steel pipe pile provided on a bridge or a pier, or a marine steel structure such as a steel caisson in which the surface of a concrete structure is covered with a steel member. Things are included. The underwater metal structure is seawater or brackish water (a liquid in which freshwater and seawater are mixed) in the so-called ebb and flow zone where submersion in the sea and exposure to the atmosphere are repeated, and in the underwater part which is constantly submerged regardless of the ebb and flow. It is provided in contact with the water, and is exposed to an environment where rust is very likely to occur.

従って、このような水中金属構造物では、長期間の使用により錆が発生し減肉して強度が低下するため、補強工事或いは取替工事等を行う必要が生じる。しかし、前記補強工事或いは取替工事には多大の費用が掛かるため、前記水中金属構造物の干満帯及び水中部では電着防食、電気防食、或いはこれらの併用により、前記水中金属構造物の寿命延長を図ることが行われている。 Therefore, in such an underwater metal structure, rust is generated by long-term use, the wall thickness is reduced, and the strength is lowered. Therefore, it is necessary to perform reinforcement work or replacement work. However, since the reinforcement work or the replacement work requires a large amount of cost, the life of the underwater metal structure can be reduced by electrodeposition corrosion protection, electrocorrosion protection, or a combination thereof in the tidal zone and the underwater part of the underwater metal structure. Extensions are being made.

従来、例えば、前記水中金属構造物の干満帯及び水中部に対し所要の間隔をあけて陽極を設け、該陽極と水中金属構造物との間に直流電源を設けて直流電流を通電することが行われている。これにより、海水に溶存するカルシウムイオン(Ca2+)やマグネシウムイオン(Mg2+)等の陽イオンが陰極としての水中金属構造物へ向かって海水中を泳動し、該水中金属構造物において電子を得る。前記水中金属構造物の干満帯及び水中部の表面には、CaCO及びMg(OH)等を主成分とする防食電着被膜(エレクトロコーティング層)が形成され、該防食電着被膜により前記水中金属構造物の干満帯及び水中部が防食されるようになっている。 Conventionally, for example, an anode may be provided at a required interval between the ebb and flow zone and the underwater portion of the underwater metal structure, and a direct current power source may be provided between the anode and the underwater metal structure to energize a direct current. It is done. As a result, cations such as calcium ions (Ca 2+ ) and magnesium ions (Mg 2+ ) dissolved in seawater migrate in the seawater toward the underwater metal structure as a cathode, and electrons are obtained in the underwater metal structure. .. An anticorrosion electrodeposition coating (electrocoating layer) containing CaCO 3 and Mg (OH) 2 as main components is formed on the surface of the ebb and flow zone and the underwater portion of the underwater metal structure, and the anticorrosion electrodeposition coating is used to form the anticorrosion electrodeposition coating. The tidal zone and the underwater part of the underwater metal structure are protected against corrosion.

更に、前述の如く水中金属構造物の干満帯及び水中部の表面に防食電着被膜を形成した後、電気防食用陽極と水中金属構造物との間に防食電流が流れるようにすることにより、水中金属構造物の電気防食(例えば、流電陽極方式の電気防食、或いは外部電源方式の電気防食がある)を行うことも提案されている。 Further, as described above, after the anticorrosion electrodeposition coating is formed on the ebb and flow zone of the underwater metal structure and the surface of the underwater part, the anticorrosion current is allowed to flow between the electrolytic anticorrosion anode and the underwater metal structure. It has also been proposed to carry out electrocorrosion protection of underwater metal structures (for example, there is electrocorrosion protection of a current current anode method or electric corrosion protection of an external power source method).

尚、水中金属構造物の電気防食と関連する一般的技術水準を示すものとしては、例えば、特許文献1がある。 As a general technical level related to electrocorrosion protection of underwater metal structures, for example, Patent Document 1 is available.

特開昭62-196384号公報Japanese Unexamined Patent Publication No. 62-196384

しかしながら、従来の場合、水中金属構造物の付近に直流電源及び該直流電源用の発電機を配置し、前記直流電源と陽極との間に配線を敷設した上で、水中金属構造物の形状に合わせた陽極を水中金属構造物と適切な間隔になるように設置し通電を行う必要があった。更に、前記発電機への燃料の補給だけでなく、直流電源の電流値及び電圧値の確認と調整をその都度実施しなければならず、通電期間を長くとることは困難となっていた。加えて施工完了後は、陽極、陽極設置用の部材、配線、直流電源、発電機を全て撤去する必要があった。これらの作業は、非常に手間と時間が掛かり、改善が望まれていた。 However, in the conventional case, a DC power supply and a generator for the DC power supply are arranged in the vicinity of the underwater metal structure, wiring is laid between the DC power supply and the anode, and then the shape of the underwater metal structure is formed. It was necessary to install the combined electrodes at an appropriate distance from the underwater metal structure and energize them. Further, not only the refueling of the generator but also the confirmation and adjustment of the current value and the voltage value of the DC power source must be carried out each time, and it is difficult to lengthen the energization period. In addition, after the construction was completed, it was necessary to remove the anode, members for installing the anode, wiring, DC power supply, and generator. These operations were very laborious and time-consuming, and improvement was desired.

又、従来の場合、水中金属構造物の形状に合わせた陽極を適切な間隔となるように精密に設置できなくなったり、或いは、直流電源の調整と管理をうまくできなくなったりすることがあった。これは、電着被膜形成において適切な電流密度分布を維持することができなくなり、電流が不足すると、電着被膜が形成されなくなることを意味する。逆に電流が過剰に流れると、水中金属構造物の表面で水素ガスが多量に発生し、電着被膜が剥離してしまうという問題もあった。 Further, in the conventional case, it may not be possible to precisely install the anodes according to the shape of the underwater metal structure at appropriate intervals, or it may not be possible to properly adjust and manage the DC power supply. This means that an appropriate current density distribution cannot be maintained in the electrodeposition film formation, and when the current is insufficient, the electrodeposition film is not formed. On the contrary, when an excessive current flows, a large amount of hydrogen gas is generated on the surface of the underwater metal structure, and there is also a problem that the electrodeposition coating is peeled off.

本開示は、上記従来の問題点に鑑みてなしたもので、直流電源や配線を不要として施工を容易に行いつつ、電着被膜を安定して形成し得る水中金属構造物の防食電着被膜形成方法を提供しようとするものである。 The present disclosure has been made in view of the above-mentioned conventional problems, and is an anticorrosion electrodeposition coating of an underwater metal structure capable of stably forming an electrodeposition coating while facilitating construction without the need for a DC power supply or wiring. It is intended to provide a forming method.

上記目的を達成するために、本開示の水中金属構造物の防食電着被膜形成方法は、水中金属構造物の表面における付着物を除去する素地調整工程と、
該素地調整工程で付着物が除去された水中金属構造物の表面に、該水中金属構造物の表面に両端部が接続される鋼製の芯材と、該芯材に被覆されるマグネシウム合金とを備えた陽極を取り付ける陽極取付工程と
を行い、
前記水中金属構造物は、凹部と凸部とが形成されるよう連結配置される鋼矢板であり、
前記陽極取付工程で、前記陽極のマグネシウム合金が水深方向へ延び且つ互いに隣接する前記凸部と凸部との間に配設されるよう、前記芯材の両端部が鋼矢板の表面に取り付けられる
In order to achieve the above object, the anticorrosion electrodeposition film forming method of the underwater metal structure of the present disclosure includes a substrate adjusting step of removing deposits on the surface of the underwater metal structure.
A steel core material in which both ends are connected to the surface of the underwater metal structure on the surface of the underwater metal structure from which deposits have been removed in the substrate adjustment step, and a magnesium alloy coated on the core material. Perform the anode mounting process and mount the anode with
The underwater metal structure is a steel sheet pile that is connected and arranged so that a concave portion and a convex portion are formed.
In the anode mounting step, both ends of the core material are attached to the surface of the steel sheet pile so that the magnesium alloy of the anode extends in the water depth direction and is disposed between the convex portions adjacent to each other. ..

前記水中金属構造物の防食電着被膜形成方法において、前記陽極取付工程は、
前記鋼矢板の表面に形成すべき電着被膜の必要膜厚tを設定する必要膜厚設定工程と、
該必要膜厚設定工程で設定された必要膜厚tに基づいて単位面積当たりの通電量iを求める単位面積通電量算出工程と、
前記鋼矢板の表面における電着被膜を形成すべき表面積Sを設定する表面積設定工程と、
該表面積設定工程で設定された表面積Sと前記単位面積通電量算出工程で求められた単位面積当たりの通電量iとに基づき必要通電量Iを求める必要通電量算出工程と、
連結配置される前記鋼矢板の凹部の数nを設定する凹部設定工程と、
前記必要通電量算出工程で求められた必要通電量Iと前記凹部設定工程で設定された凹部の数nとに基づき前記鋼矢板の凹部一個当たりの凹部通電量Iを求める凹部通電量算出工程と、
前記陽極の一本当たりの発生電流iを設定する陽極発生電流設定工程と、
前記凹部通電量算出工程で求められた凹部通電量Iと前記陽極発生電流設定工程で設定された発生電流iとに基づき前記鋼矢板の凹部一個に取り付けるべき陽極の本数Yを求める陽極本数設定工程と
を含むようにすることができる。
In the method for forming an anticorrosion electrodeposition film on an underwater metal structure, the anode mounting step is
The required film thickness setting step for setting the required film thickness t of the electrodeposition film to be formed on the surface of the steel sheet pile, and the required film thickness setting step.
A unit area energization amount calculation step for obtaining an energization amount i per unit area based on the required film thickness t set in the required film thickness setting step, and a unit area energization amount calculation step.
A surface area setting step for setting a surface area S on which an electrodeposition coating is to be formed on the surface of the steel sheet pile, and a surface area setting step.
The required energization amount calculation step of obtaining the required energization amount I based on the surface area S set in the surface area setting step and the energization amount i per unit area obtained in the unit area energization amount calculation step.
A recess setting step for setting the number n of recesses of the steel sheet piles to be connected and arranged, and a recess setting step.
Recessed energization amount calculation step for obtaining the recess energizing amount Io per recess of the steel sheet pile based on the required energizing amount I obtained in the required energizing amount calculation step and the number n of recesses set in the recess setting step. When,
The anode generating current setting step of setting the generated current yy per anode and the anode generating current setting step.
The number of anodes Y to be attached to one recess of the steel sheet pile is obtained based on the recess energization amount Io obtained in the recess energization amount calculation step and the generated current ii set in the anode generation current setting step. It can be included with the setting process.

前記水中金属構造物の防食電着被膜形成方法において、前記陽極取付工程で、前記芯材の両端部は、前記鋼矢板の凸部の表面に取り付けられるようにすることができる。 In the method for forming an anticorrosion electrodeposition film on an underwater metal structure, both ends of the core material can be attached to the surface of the convex portion of the steel sheet pile in the anode attaching step.

前記水中金属構造物の防食電着被膜形成方法において、前記陽極取付工程で、前記芯材の両端部は、前記鋼矢板の凸部の表面に固着されたブラケットに対し締結部材により着脱自在に取り付けられるようにすることができる。 In the method for forming an anticorrosion electrodeposition film on an underwater metal structure, both ends of the core material are detachably attached to a bracket fixed to the surface of the convex portion of the steel sheet pile by a fastening member in the anode mounting step. Can be done.

本発明の水中金属構造物の防食電着被膜形成方法によれば、直流電源や配線を不要として施工を容易に行いつつ、電着被膜を安定して形成し得るという優れた効果を奏し得る。 According to the method for forming an anticorrosion electrodeposition coating on an underwater metal structure of the present invention, it is possible to obtain an excellent effect that an electrodeposition coating can be stably formed while facilitating construction without the need for a DC power supply or wiring.

本発明の水中金属構造物の防食電着被膜形成方法の実施例を示すフローチャートである。It is a flowchart which shows the Example of the anticorrosion electrodeposition film formation method of the underwater metal structure of this invention. 本発明の水中金属構造物の防食電着被膜形成方法の実施例における陽極を示す概要構成平面図である。It is a schematic structural plan view which shows the anode in the Example of the anticorrosion electrodeposition film formation method of the underwater metal structure of this invention. 本発明の水中金属構造物の防食電着被膜形成方法の実施例における陽極を示す概要構成正面図である。It is a schematic structural front view which shows the anode in the Example of the anticorrosion electrodeposition film formation method of the underwater metal structure of this invention. 本発明の水中金属構造物の防食電着被膜形成方法の実施例における必要膜厚と単位面積当たりの通電量との関係を示す線図である。It is a diagram which shows the relationship between the required film thickness and the energization amount per unit area in the Example of the anticorrosion electrodeposition film formation method of the underwater metal structure of this invention. 本発明の水中金属構造物の防食電着被膜形成方法の実施例における陽極の設置に関する変形例を示す要部拡大正面図である。It is an enlarged front view of the main part which shows the modification about the installation of the anode in the Example of the anticorrosion electrodeposition film formation method of the underwater metal structure of this invention.

以下、本発明の実施の形態を添付図面を参照して説明する。 Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings.

図1~図4は本発明の水中金属構造物の防食電着被膜形成方法の実施例である。 1 to 4 are examples of the method for forming an anticorrosion electrodeposition film on an underwater metal structure of the present invention.

本実施例の場合、図1に示す如く、素地調整工程(ステップS100)と、陽極取付工程(ステップS200)とを行うようになっている。 In the case of this embodiment, as shown in FIG. 1, the substrate adjusting step (step S100) and the anode mounting step (step S200) are performed.

前記素地調整工程は、水中金属構造物10の表面における貝類等の海生生物や錆といった付着物を除去する工程である。前記素地調整工程には、ノズルから高圧水を水中金属構造物10の表面に噴射する高圧水洗浄、或いは、ノズルから砂や金属等の研掃材を水中金属構造物10の表面に噴射するショットブラストを採用することができる。 The substrate adjusting step is a step of removing marine organisms such as shellfish and deposits such as rust on the surface of the underwater metal structure 10. In the substrate adjustment step, high-pressure water cleaning is performed by injecting high-pressure water from the nozzle onto the surface of the underwater metal structure 10, or a shot in which a polishing material such as sand or metal is injected from the nozzle onto the surface of the underwater metal structure 10. Blasting can be adopted.

前記陽極取付工程は、前記素地調整工程で付着物が除去された水中金属構造物10の表面に、陽極20を取り付ける工程である。 The anode mounting step is a step of mounting the anode 20 on the surface of the underwater metal structure 10 from which deposits have been removed in the substrate adjusting step.

前記陽極20は、図2及び図3に示す如く、前記水中金属構造物10の表面に両端部が接続される鋼製の芯材21と、該芯材21の中間部外周に被覆されるマグネシウム合金22とを備えている。尚、前記芯材21は、前記マグネシウム合金22が被覆される中間部の上下端部を屈曲させた形状としてある。又、図2の実施例では、海洋鋼構造物を含む水中金属構造物10として岸壁に設けられる鋼矢板11を示している。前記岸壁は、上下方向へ延び且つ該上下方向と交差する幅方向(水平方向)へ延びる壁面を備え、前記鋼矢板11は、前記壁面に沿って凹部11a及び凸部11bが前記幅方向へ交互に形成されるよう連結配置され、図3に示す如く、水中の深さ方向へ垂下している。 As shown in FIGS. 2 and 3, the anode 20 has a steel core material 21 whose both ends are connected to the surface of the underwater metal structure 10 and magnesium coated on the outer periphery of the intermediate portion of the core material 21. It is provided with an alloy 22. The core material 21 has a shape in which the upper and lower ends of the intermediate portion covered with the magnesium alloy 22 are bent. Further, in the embodiment of FIG. 2, a steel sheet pile 11 provided on the quay as an underwater metal structure 10 including a marine steel structure is shown. The quay has a wall surface extending in the vertical direction and extending in the width direction (horizontal direction) intersecting the vertical direction, and the steel sheet pile 11 has concave portions 11a and convex portions 11b alternating in the width direction along the wall surface. It is connected and arranged so as to be formed in the water, and as shown in FIG. 3, it hangs down in the depth direction of the water.

前記陽極取付工程では、前記陽極20のマグネシウム合金22が水深方向へ延び且つ前記凸部11bと凸部11bとの間、即ち互いに隣接する凸部11b間に配設されるよう、前記芯材21の両端部が鋼矢板11の表面に取り付けられるようになっている。 In the anode mounting step, the core material 21 is arranged so that the magnesium alloy 22 of the anode 20 extends in the water depth direction and is disposed between the convex portions 11b and the convex portions 11b, that is, between the convex portions 11b adjacent to each other. Both ends of the steel sheet pile 11 are attached to the surface of the steel sheet pile 11.

前記陽極取付工程は、より詳細には、図1に示す如く、必要膜厚設定工程(ステップS210)と、単位面積通電量算出工程(ステップS220)と、表面積設定工程(ステップS230)と、必要通電量算出工程(ステップS240)と、凹部設定工程(ステップS250)と、凹部通電量算出工程(ステップS260)と、陽極発生電流設定工程(ステップS270)と、陽極本数設定工程(ステップS280)とを含んでいる。 More specifically, as shown in FIG. 1, the anode mounting step requires a required film thickness setting step (step S210), a unit area energization amount calculation step (step S220), and a surface surface setting step (step S230). The energization amount calculation step (step S240), the recess setting step (step S250), the recess energization amount calculation step (step S260), the anode generation current setting step (step S270), and the number of anodes setting step (step S280). Includes.

前記必要膜厚設定工程は、前記鋼矢板11の表面に形成すべき電着被膜の必要膜厚tを設定する工程である。 The required film thickness setting step is a step of setting the required film thickness t of the electrodeposition film to be formed on the surface of the steel sheet pile 11.

前記単位面積通電量算出工程は、前記必要膜厚設定工程で設定された必要膜厚tに基づいて単位面積当たりの通電量iを求める工程である。 The unit area energization amount calculation step is a step of obtaining the energization amount i per unit area based on the required film thickness t set in the required film thickness setting step.

前記表面積設定工程は、前記鋼矢板11の表面における電着被膜を形成すべき表面積Sを設定する工程である。 The surface area setting step is a step of setting a surface area S on which an electrodeposition coating is to be formed on the surface of the steel sheet pile 11.

前記必要通電量算出工程は、前記表面積設定工程で設定された表面積Sと前記単位面積通電量算出工程で求められた単位面積当たりの通電量iとに基づき必要通電量I(=i×S)を求める工程である。 In the required energization amount calculation step, the required energization amount I (= i × S) is based on the surface area S set in the surface area setting step and the energization amount i per unit area obtained in the unit area energization amount calculation step. Is the process of finding.

前記凹部設定工程は、連結配置される前記鋼矢板11の凹部11aの数nを設定する工程である。 The recess setting step is a step of setting the number n of the recesses 11a of the steel sheet pile 11 to be connected and arranged.

前記凹部通電量算出工程は、前記必要通電量算出工程で求められた必要通電量Iと前記凹部設定工程で設定された凹部11aの数nとに基づき前記鋼矢板11の凹部11a一個当たりの凹部通電量I(=I/n)を求める工程である。 In the recess energization amount calculation step, the recesses per recess 11a of the steel sheet pile 11 are based on the required energization amount I obtained in the required energization amount calculation step and the number n of the recesses 11a set in the recess setting step. This is a step of obtaining the energization amount I o (= I / n).

前記陽極発生電流設定工程は、前記陽極20の一本当たりの発生電流iを設定する工程である。 The anode generated current setting step is a step of setting the generated current yy per anode 20.

前記陽極本数設定工程は、前記凹部通電量算出工程で求められた凹部通電量Iと前記陽極発生電流設定工程で設定された発生電流iとに基づき前記鋼矢板11の凹部11a一個に取り付けるべき陽極20の本数Y(=I/i)を求める工程である。 The number of anodes setting step is attached to one recess 11a of the steel sheet pile 11 based on the recess energization amount Io obtained in the recess energization amount calculation step and the generated current i set in the anode generation current setting step. This is a step of obtaining the number Y (= I o / i y ) of the power anodes 20.

前記陽極取付工程で、前記芯材21の両端部は、図2及び図3に示す如く、前記鋼矢板11の凸部11bの表面に対し溶接等で取り付けられるようになっている。但し、前記芯材21の両端部を、図2の仮想線で示す如く、前記鋼矢板11の凹部11aの表面に取り付けることも可能である。要は、前記マグネシウム合金22の位置(水深方向へ延び且つ互いに隣接する前記凸部11bと凸部11bとの間に配設される位置)が重要であり、原理上、陽極20の芯材21は鋼矢板11と電気的に接触していれば良く、芯材21の取り付け位置はどこでも良い。 In the anode mounting step, both ends of the core material 21 are attached to the surface of the convex portion 11b of the steel sheet pile 11 by welding or the like, as shown in FIGS. 2 and 3. However, both ends of the core material 21 can be attached to the surface of the recess 11a of the steel sheet pile 11 as shown by the virtual line in FIG. In short, the position of the magnesium alloy 22 (the position extending in the water depth direction and arranged between the convex portions 11b and the convex portions 11b adjacent to each other) is important, and in principle, the core material 21 of the anode 20 It is sufficient that the steel sheet pile 11 is in electrical contact with the steel sheet pile 11, and the core material 21 may be attached at any position.

次に、上記実施例の作用を説明する。 Next, the operation of the above embodiment will be described.

先ず、図1のステップS100で示す素地調整工程において、図2及び図3に示す水中金属構造物10である鋼矢板11の表面における付着物(例えば、貝類等の海生生物や錆)が除去される。前記素地調整工程に、例えば、高圧水洗浄を採用した場合、図示していないノズルから高圧水が前記鋼矢板11の表面に噴射される。又、前記素地調整工程に、例えば、ショットブラストを採用した場合、図示していないノズルから砂や金属等の研掃材が前記鋼矢板11の表面に噴射される。 First, in the substrate adjusting step shown in step S100 of FIG. 1, deposits (for example, marine organisms such as shellfish and rust) on the surface of the steel sheet pile 11 which is the underwater metal structure 10 shown in FIGS. 2 and 3 are removed. Will be done. When, for example, high-pressure water washing is adopted in the substrate adjusting step, high-pressure water is sprayed onto the surface of the steel sheet pile 11 from a nozzle (not shown). Further, when, for example, shot blasting is adopted in the substrate adjusting step, a polishing material such as sand or metal is sprayed onto the surface of the steel sheet pile 11 from a nozzle (not shown).

続いて、図1のステップS200で示す陽極取付工程において、前記素地調整工程で付着物が除去された鋼矢板11の表面に陽極20が取り付けられる。 Subsequently, in the anode mounting step shown in step S200 of FIG. 1, the anode 20 is mounted on the surface of the steel sheet pile 11 from which the deposits have been removed in the substrate adjusting step.

前記鋼矢板11の凹部11a一個に取り付けるべき陽極20の本数Yに関しては、以下の工程、即ち、必要膜厚設定工程と、単位面積通電量算出工程と、表面積設定工程と、必要通電量算出工程と、凹部設定工程と、凹部通電量算出工程と、陽極発生電流設定工程と、陽極本数設定工程とを順次行うことで設定される。 Regarding the number Y of the anodes 20 to be attached to one recess 11a of the steel sheet pile 11, the following steps, that is, a required film thickness setting step, a unit area energization amount calculation step, a surface surface setting step, and a required energization amount calculation step. , The recess setting step, the recess energization amount calculation step, the anode generation current setting step, and the number of anodes setting step are sequentially performed.

前記陽極取付工程における図1のステップS210で示す必要膜厚設定工程において、前記鋼矢板11の表面に形成すべき電着被膜の必要膜厚tが設定される。前記電着被膜の必要膜厚tは、例えば、500[μm]程度とすれば良い。 In the required film thickness setting step shown in step S210 of FIG. 1 in the anode mounting step, the required film thickness t of the electrodeposition film to be formed on the surface of the steel sheet pile 11 is set. The required film thickness t of the electrodeposition film may be, for example, about 500 [μm].

前記陽極取付工程における図1のステップS220で示す単位面積通電量算出工程において、前記必要膜厚設定工程で設定された必要膜厚tに基づいて単位面積当たりの通電量iが求められる。 In the unit area energization amount calculation step shown in step S220 of FIG. 1 in the anode mounting step, the energization amount i per unit area is obtained based on the required film thickness t set in the required film thickness setting step.

ここで、前記必要膜厚tと単位面積当たりの通電量iとの関係は、図4に示す線図のようになる。このため、前記必要膜厚がt=500[μm]であれば、前記単位面積当たりの通電量はi≒30[A・day/m]となる。 Here, the relationship between the required film thickness t and the energization amount i per unit area is as shown in the diagram shown in FIG. Therefore, if the required film thickness is t = 500 [μm], the energization amount per unit area is i≈30 [A.day / m 2 ].

前記陽極取付工程における図1のステップS230で示す表面積設定工程において、前記鋼矢板11の表面における電着被膜を形成すべき表面積Sが設定される。前記鋼矢板11の凹部11aと凸部11bとを平面に引き延ばしたと仮定したときの幅が、例えば、W=20[m]で、高さがH=5[m]である場合、前記表面積はS=W・H=20×5=100[m]となる。 In the surface area setting step shown in step S230 of FIG. 1 in the anode mounting step, the surface area S on which the electrodeposition film is to be formed on the surface of the steel sheet pile 11 is set. When it is assumed that the concave portion 11a and the convex portion 11b of the steel sheet pile 11 are stretched in a plane, the surface area is, for example, W = 20 [m] and the height is H = 5 [m]. S = WH = 20 × 5 = 100 [m 2 ].

前記陽極取付工程における図1のステップS240で示す必要通電量算出工程において、前記表面積設定工程で設定された表面積Sと前記単位面積通電量算出工程で求められた単位面積当たりの通電量iとに基づき必要通電量Iが求められる。前記通電量がi=30[A・day/m]で、表面積がS=100[m]である場合、前記必要通電量はI=i×S=30×100=3000[A・day]となる。 In the required energization amount calculation step shown in step S240 of FIG. 1 in the anode mounting step, the surface area S set in the surface area setting step and the energization amount i per unit area obtained in the unit area energization amount calculation step are set. Based on this, the required energization amount I is obtained. When the energization amount is i = 30 [A ・ day / m 2 ] and the surface area is S = 100 [m 2 ], the required energization amount is I = i × S = 30 × 100 = 3000 [A ・ day]. ].

前記陽極取付工程における図1のステップS250で示す凹部設定工程において、連結配置される前記鋼矢板11の凹部11aの数nが設定される。前記鋼矢板11の凹部11aの数は、例えば、n=20と設定される。 In the recess setting step shown in step S250 of FIG. 1 in the anode mounting step, the number n of the recesses 11a of the steel sheet pile 11 to be connected and arranged is set. The number of recesses 11a of the steel sheet pile 11 is set to, for example, n = 20.

前記陽極取付工程における図1のステップS260で示す凹部通電量算出工程において、前記必要通電量算出工程で求められた必要通電量Iと前記凹部設定工程で設定された凹部11aの数nとに基づき前記鋼矢板11の凹部11a一個当たりの凹部通電量Iが求められる。前記必要通電量がI=3000[A・day]で、前記鋼矢板11の凹部11aの数がn=20である場合、前記鋼矢板11の凹部11a一個当たりの凹部通電量はI=I/n=3000/20=150[A・day]となる。 In the recess energization amount calculation step shown in step S260 of FIG. 1 in the anode mounting step, based on the required energization amount I obtained in the required energization amount calculation step and the number n of the recesses 11a set in the recess setting step. The recess energization amount Io per recess 11a of the steel sheet pile 11 is obtained. When the required energization amount is I = 3000 [A · day] and the number of recesses 11a of the steel sheet pile 11 is n = 20, the recess energization amount per recess 11a of the steel sheet pile 11 is I o = I. / N = 3000/20 = 150 [A · day].

前記陽極取付工程における図1のステップS270で示す陽極発生電流設定工程において、前記陽極20の一本当たりの発生電流iが設定される。前記陽極20の一本当たりの発生電流は、前記マグネシウム合金22の物量に比例し、例えば、i=150[A・day]と設定される。 In the anode generation current setting step shown in step S270 of FIG. 1 in the anode mounting step, the generated current yy per anode 20 is set. The generated current per anode 20 is proportional to the physical quantity of the magnesium alloy 22, and is set, for example, i y = 150 [A. Day].

前記陽極取付工程における図1のステップS280で示す陽極本数設定工程において、前記凹部通電量算出工程で求められた凹部通電量Iと前記陽極発生電流設定工程で設定された発生電流iとに基づき前記鋼矢板11の凹部11a一個に取り付けるべき陽極20の本数Yが求められる。前記凹部通電量がI=150[A・day]で、前記発生電流がi=150[A・day]である場合、前記陽極20の本数は、Y=I/i=150/150=1[本]となる。 In the process of setting the number of anodes shown in step S280 of FIG. 1 in the anode mounting step, the concave current energization amount Io obtained in the concave energization amount calculation step and the generated current i set in the anode generated current setting step are set. Based on this, the number Y of the anodes 20 to be attached to one recess 11a of the steel sheet pile 11 is obtained. When the concave energization amount is I o = 150 [A · day] and the generated current is i y = 150 [A · day], the number of the anodes 20 is Y = I o / i y = 150 /. 150 = 1 [book].

そして、前記陽極取付工程における陽極本数設定工程で、前記鋼矢板11の凹部11a一個に取り付けるべき陽極20の本数Yが求められると、該陽極20の芯材21の両端部は、図2及び図3に示す如く、前記鋼矢板11の凸部11bの表面に対し溶接等で取り付けられる。尚、図3には、前記鋼矢板11の凹部11a一個に一本の陽極20を取り付けた例を示している。仮に、前記発生電流がi=75[A・day]である場合、前記陽極20の本数は、Y=I/i=150/75=2[本]となるため、前記鋼矢板11の凹部11a一個に対して二本の陽極20が上下方向へ直列に配設されるよう、該陽極20を取り付ければ良い。又、前記発生電流がi=50[A・day]である場合、前記陽極20の本数は、Y=I/i=150/50=3[本]となるため、前記鋼矢板11の凹部11a一個に対して三本の陽極20が上下方向へ直列に配設されるよう、該陽極20を取り付ければ良い。 Then, when the number Y of the anodes 20 to be attached to one recess 11a of the steel sheet pile 11 is obtained in the anode number setting step in the anode attaching step, both ends of the core material 21 of the anode 20 are shown in FIGS. 2 and 2. As shown in 3, the steel sheet pile 11 is attached to the surface of the convex portion 11b by welding or the like. Note that FIG. 3 shows an example in which one anode 20 is attached to one recess 11a of the steel sheet pile 11. If the generated current is i y = 75 [A · day], the number of the anodes 20 is Y = I o / i y = 150/75 = 2 [lines], so that the steel sheet pile 11 The anode 20 may be attached so that two anodes 20 are arranged in series in the vertical direction with respect to one recess 11a of the above. Further, when the generated current is i y = 50 [A · day], the number of the anodes 20 is Y = I o / i y = 150/50 = 3 [lines], so that the steel sheet pile 11 The anode 20 may be attached so that three anodes 20 are arranged in series in the vertical direction with respect to one recess 11a.

ここで、実際の作業として、前記鋼矢板11への芯材21の取り付けは、潜水士或いはドライ工法による鋼矢板11の表面の素地調整と水中での溶接等によって行われる。このため、前記鋼矢板11の凹部11aに対して芯材21を取り付けるより、該芯材21を凸部11bの表面に取り付ける方が、作業性を向上する上で好ましい。因みに、前記ドライ工法とは、鋼矢板11の干満帯に止水箱を取り付け、該止水箱の内部の水をポンプで排出し、ドライ状態で作業を行えるようにする工法である。 Here, as an actual work, the core material 21 is attached to the steel sheet pile 11 by adjusting the surface of the steel sheet pile 11 by a diver or a dry method, welding in water, or the like. Therefore, it is preferable to attach the core material 21 to the surface of the convex portion 11b rather than attaching the core material 21 to the concave portion 11a of the steel sheet pile 11 in order to improve workability. Incidentally, the dry method is a method in which a water stop box is attached to the tidal zone of the steel sheet pile 11 and the water inside the water stop box is discharged by a pump so that the work can be performed in a dry state.

前記素地調整工程を経た鋼矢板11の表面には、付着物がなく、前記陽極取付工程で取り付けられた陽極20により電気が均一に流れるため、該陽極20のマグネシウム合金22が溶解して消失するまで、電着被膜形成において必要となる電流密度分布が安定して維持される。これにより、鋼矢板11に対し均一な電流密度分布でカソード電流が流れ、割れや剥がれのない電着被膜が必要膜厚tとなるまで形成される。又、前記素地調整工程を行うことは、鋼矢板11の状態、即ち、厚さの変化や孔の有無等を確認する上でも有効となる。 There are no deposits on the surface of the steel sheet pile 11 that has undergone the substrate adjustment step, and electricity flows uniformly through the anode 20 attached in the anode mounting step, so that the magnesium alloy 22 of the anode 20 melts and disappears. Until then, the current density distribution required for forming the electrodeposition film is stably maintained. As a result, the cathode current flows through the steel sheet pile 11 with a uniform current density distribution, and an electrodeposition film without cracking or peeling is formed until the required film thickness t is reached. Further, performing the substrate adjusting step is also effective in confirming the state of the steel sheet pile 11, that is, the change in thickness, the presence or absence of holes, and the like.

本実施例の場合、従来に比べ、水中金属構造物10の付近に直流電源及び該直流電源用の発電機を配置し、前記直流電源と陽極との間に配線を敷設した上で、水中金属構造物10の形状に合わせた陽極を水中金属構造物10と適切な間隔になるように設置し通電を行う必要がなくなる。更に、前記発電機への燃料の補給や、直流電源の電流値及び電圧値の確認と調整をその都度実施しなくて済み、通電期間を長くしても問題はない。加えて施工完了後に、陽極、陽極設置用の部材、配線、直流電源、発電機を撤去する必要もない。このように、本実施例では、水中金属構造物10の表面の素地調整を行った後に陽極20を取り付けるだけで電着被膜を形成可能となり、通電中の作業が一切不要となることから、電着被膜形成のための通電期間に関する制約がなくなる。このため、水中金属構造物10の表面における電流密度がバラついて電流密度が低い箇所があったとしても、通電期間を長くとれば必要膜厚tの電着被膜を安定して得ることが可能となる。更に、マグネシウム合金22を備えた陽極20を用いて通電している期間中は、水中金属構造物10の表面への電流印加により、電着被膜の形成と同時に、水中金属構造物10の表面は電気防食もなされていると考えられる。 In the case of this embodiment, as compared with the conventional case, a DC power supply and a generator for the DC power supply are arranged in the vicinity of the underwater metal structure 10, wiring is laid between the DC power supply and the anode, and then the underwater metal is used. It is not necessary to install an anode matching the shape of the structure 10 at an appropriate distance from the underwater metal structure 10 to energize the structure 10. Further, it is not necessary to refuel the generator and check and adjust the current value and the voltage value of the DC power source each time, and there is no problem even if the energization period is lengthened. In addition, it is not necessary to remove the anode, members for installing the anode, wiring, DC power supply, and generator after the construction is completed. As described above, in this embodiment, the electrodeposition film can be formed only by attaching the anode 20 after adjusting the substrate of the surface of the underwater metal structure 10, and the work during energization is not required at all. There are no restrictions on the energization period for forming a film. Therefore, even if the current density on the surface of the underwater metal structure 10 varies and the current density is low, it is possible to stably obtain an electrodeposition coating having a required thickness t by extending the energization period. Become. Further, during the period of energization using the anode 20 provided with the magnesium alloy 22, the surface of the underwater metal structure 10 is formed at the same time as the electrodeposition film is formed by applying a current to the surface of the underwater metal structure 10. It is thought that electric corrosion protection is also provided.

又、本実施例の場合、従来とは異なり、水中金属構造物10の形状に合わせた陽極を適切な間隔となるように精密に設置したり、或いは、直流電源の調整と管理をしたりしなくて済み、電着被膜形成において適切な電流密度分布を維持することができる。このため、電流が不足して、電着被膜が形成されなくなる心配はない。逆に電流が過剰に流れて水中金属構造物10の表面で水素ガスが多量に発生し、電着被膜が剥離してしまう心配もない。 Further, in the case of this embodiment, unlike the conventional case, anodes matching the shape of the underwater metal structure 10 are precisely installed at appropriate intervals, or the DC power supply is adjusted and managed. It is not necessary, and an appropriate current density distribution can be maintained in the formation of the electrodeposition film. Therefore, there is no concern that the electrodeposition film will not be formed due to insufficient current. On the contrary, there is no concern that an excessive current flows and a large amount of hydrogen gas is generated on the surface of the underwater metal structure 10 and the electrodeposition coating is peeled off.

更に又、仮に、前記素地調整工程を行わずに陽極20を設置した場合、錆の上から電着被膜が形成されるため、該電着被膜が錆ごと剥離する懸念があり、電着被膜の密着性が低いと言える。しかし、本実施例の場合、前記素地調整工程により鋼矢板11の表面から前記付着物が除去されることで、鋼矢板11の素地表面に充分な密着性を有する電着被膜を形成することができ、長期に亘る防食作用が発揮できる。更に電気抵抗となる錆が除去されることで、陽極20のマグネシウム合金22の溶解が促進されて、該マグネシウム合金22が消失するまでのいわゆる耐用年数が短くなり、鋼矢板11の表面に必要膜厚tの電着被膜が形成されるまでの通電期間が比較的短くて済む。 Furthermore, if the anode 20 is installed without performing the substrate adjustment step, an electrodeposition film is formed on the rust, and there is a concern that the electrodeposition film may be peeled off together with the rust. It can be said that the adhesion is low. However, in the case of this embodiment, the deposits are removed from the surface of the steel sheet pile 11 by the base material adjusting step, so that an electrodeposition coating having sufficient adhesion can be formed on the base material surface of the steel sheet pile 11. It can exert a long-term anticorrosion effect. Further, by removing the rust that becomes an electric resistance, the dissolution of the magnesium alloy 22 of the anode 20 is promoted, the so-called useful life until the magnesium alloy 22 disappears is shortened, and the required film on the surface of the steel sheet pile 11 is shortened. The energization period until the electrodeposition film having a thickness of t is formed can be relatively short.

こうして、直流電源や配線を不要として施工を容易に行いつつ、電着被膜を安定して形成し得る。 In this way, the electrodeposition coating can be stably formed while the construction can be easily performed without the need for a DC power supply or wiring.

図5は本発明の水中金属構造物10の防食電着被膜形成方法の実施例における陽極の設置に関する変形例であって、図中、図2及び図3と同一の符号を付した部分は同一物を表わしている。 FIG. 5 is a modified example of the installation of the anode in the embodiment of the method for forming an anticorrosion electrodeposition film of the underwater metal structure 10 of the present invention, and in the drawings, the portions with the same reference numerals as those in FIGS. 2 and 3 are the same. It represents an object.

図5に示す変形例は、前記陽極取付工程で、前記芯材21の両端部が、前記鋼矢板11の凸部11bの表面に固着されたブラケット30に対しボルト・ナット等の締結部材40により着脱自在に取り付けられるようにしたものである。尚、図5には、前記芯材21の上側の端部のみを示し、下側の端部は省略している。又、前記締結部材40は、着脱できるものであれば、ボルト・ナット以外のものでも良い。 In the modified example shown in FIG. 5, in the anode mounting step, both ends of the core material 21 are attached to the bracket 30 fixed to the surface of the convex portion 11b of the steel sheet pile 11 by a fastening member 40 such as a bolt or a nut. It is designed so that it can be attached and detached. Note that FIG. 5 shows only the upper end portion of the core material 21, and the lower end portion is omitted. Further, the fastening member 40 may be a member other than bolts and nuts as long as it can be attached and detached.

図5に示す変形例の場合、陽極20のマグネシウム合金22が溶解して消失した後、前記芯材21の両端部から締結部材40を緩めると、ブラケット30から芯材21を取り外すことが可能となる。これにより、前記陽極20の交換を容易に行うことができ、作業性を高めることが可能となる。 In the case of the modification shown in FIG. 5, after the magnesium alloy 22 of the anode 20 is melted and disappears, the core material 21 can be removed from the bracket 30 by loosening the fastening members 40 from both ends of the core material 21. Become. As a result, the anode 20 can be easily replaced, and workability can be improved.

そして、図1~図4の実施例の場合、図2及び図3に示す如く、前記水中金属構造物10は、凹部11aと凸部11bとが形成されるよう連結配置される鋼矢板11であり、前記陽極取付工程で、前記陽極20のマグネシウム合金22が水深方向へ延び且つ互いに隣接する前記凸部11bと凸部11bとの間に配設されるよう、前記芯材21の両端部が鋼矢板11の表面に取り付けられる。このように構成すると、水中金属構造物10としての鋼矢板11の表面に対する電着被膜の形成を安定して行うことができる。 Then, in the case of the embodiments of FIGS. 1 to 4, as shown in FIGS. 2 and 3, the underwater metal structure 10 is a steel sheet pile 11 which is connected and arranged so that the concave portion 11a and the convex portion 11b are formed. In the anode mounting step, both ends of the core material 21 are provided so that the magnesium alloy 22 of the anode 20 extends in the water depth direction and is disposed between the convex portions 11b and the convex portions 11b adjacent to each other. It is attached to the surface of the steel sheet pile 11. With this configuration, the electrodeposition film can be stably formed on the surface of the steel sheet pile 11 as the underwater metal structure 10.

又、図1に示す如く、前記陽極取付工程は、前記鋼矢板11の表面に形成すべき電着被膜の必要膜厚tを設定する必要膜厚設定工程と、該必要膜厚設定工程で設定された必要膜厚tに基づいて単位面積当たりの通電量iを求める単位面積通電量算出工程と、前記鋼矢板11の表面における電着被膜を形成すべき表面積Sを設定する表面積設定工程と、該表面積設定工程で設定された表面積Sと前記単位面積通電量算出工程で求められた単位面積当たりの通電量iとに基づき必要通電量I(=i×S)を求める必要通電量算出工程と、連結配置される前記鋼矢板11の凹部11aの数nを設定する凹部設定工程と、前記必要通電量算出工程で求められた必要通電量Iと前記凹部設定工程で設定された凹部11aの数nとに基づき前記鋼矢板11の凹部11a一個当たりの凹部通電量I(=I/n)を求める凹部通電量算出工程と、前記陽極20の一本当たりの発生電流iを設定する陽極発生電流設定工程と、前記凹部通電量算出工程で求められた凹部通電量Iと前記陽極発生電流設定工程で設定された発生電流iとに基づき前記鋼矢板11の凹部11a一個に取り付けるべき陽極20の本数Y(=I/i)を求める陽極本数設定工程とを含む。このように構成すると、陽極20の本数Yを適正に選定して鋼矢板11の表面に取り付けることにより、必要膜厚tの電着被膜を安定して得ることができる。 Further, as shown in FIG. 1, the anode mounting step is set in the required film thickness setting step for setting the required film thickness t to be formed on the surface of the steel sheet pile 11 and the required film thickness setting step. A unit area energization amount calculation step for obtaining the energization amount i per unit area based on the required required film thickness t, and a surface area setting step for setting the surface surface S on which the electrodeposition film is to be formed on the surface of the steel sheet pile 11. The required energization amount calculation step of obtaining the required energization amount I (= i × S) based on the surface surface S set in the surface surface setting step and the energization amount i per unit area obtained in the unit area energization amount calculation step. , The number n of the recesses 11a of the steel sheet pile 11 to be connected and arranged, the required current amount I obtained in the recess setting step, the required current amount calculation step, and the number of recesses 11a set in the recess setting step. A recess energization amount calculation step for obtaining the recess energization amount I o (= I / n) per recess 11a of the steel sheet pile 11 based on n, and an anode for setting the generated current yy per recess 20. It should be attached to one recess 11a of the steel sheet pile 11 based on the generated current setting step, the recess energization amount Io obtained in the recess energization amount calculation step, and the generated current i set in the anode generated current setting step. It includes a step of setting the number of anodes for obtaining the number Y (= I o / i y ) of the number of anodes 20. With this configuration, the electrodeposition film having the required film thickness t can be stably obtained by appropriately selecting the number Y of the anodes 20 and attaching them to the surface of the steel sheet pile 11.

又、前記陽極取付工程で、図2及び図3に示す如く、前記芯材21の両端部は、前記鋼矢板11の凸部11bの表面に取り付けられる。このように構成すると、前記鋼矢板11の凹部11aに対して芯材21を取り付けるのに比べ、作業性を向上させることができる。 Further, in the anode mounting step, as shown in FIGS. 2 and 3, both ends of the core material 21 are mounted on the surface of the convex portion 11b of the steel sheet pile 11. With this configuration, workability can be improved as compared with attaching the core material 21 to the recess 11a of the steel sheet pile 11.

更に又、前記陽極取付工程で、図5に示す如く、前記芯材21の両端部は、前記鋼矢板11の凸部11bの表面に固着されたブラケット30に対し締結部材40により着脱自在に取り付けられる。このように構成すると、前記陽極20の交換を容易に行って作業性を高める上で有効となる。 Furthermore, in the anode mounting step, as shown in FIG. 5, both ends of the core material 21 are detachably attached to the bracket 30 fixed to the surface of the convex portion 11b of the steel sheet pile 11 by the fastening member 40. Be done. With such a configuration, it is effective to easily replace the anode 20 and improve workability.

因みに、特許文献1には、海中部における鋼管杭の表面に、アルミニウム合金、亜鉛合金、マグネシウム合金等の流電陽極を、その鋼製芯金を溶接することによって取り付ける点が記載されている。しかしながら、特許文献1には、素地調整や鋼矢板に対する具体的な陽極の設置に関する記載は何らなされていない。 Incidentally, Patent Document 1 describes that a galvanic anode of an aluminum alloy, a zinc alloy, a magnesium alloy or the like is attached to the surface of a steel pipe pile in the sea by welding a steel core metal thereof. However, Patent Document 1 does not provide any description regarding substrate adjustment or installation of a specific anode on a steel sheet pile.

尚、本発明の水中金属構造物の防食電着被膜形成方法は、上述の実施例にのみ限定されるものではなく、本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。 The method for forming an anticorrosion electrodeposition film on an underwater metal structure of the present invention is not limited to the above-described embodiment, and it goes without saying that various changes can be made without departing from the gist of the present invention. be.

10 水中金属構造物
11 鋼矢板
11a 凹部
11b 凸部
20 陽極
21 芯材
22 マグネシウム合金
30 ブラケット
40 締結部材
10 Underwater metal structure 11 Steel sheet pile 11a Concave part 11b Convex part 20 Anode 21 Core material 22 Magnesium alloy 30 Bracket 40 Fastening member

Claims (4)

水中金属構造物の表面における付着物を除去する素地調整工程と、
該素地調整工程で付着物が除去された水中金属構造物の表面に、該水中金属構造物の表面に両端部が接続される鋼製の芯材と、該芯材に被覆されるマグネシウム合金とを備えた陽極を取り付ける陽極取付工程と
を行い、
前記水中金属構造物は、凹部と凸部とが形成されるよう連結配置される鋼矢板であり、
前記陽極取付工程で、前記陽極のマグネシウム合金が水深方向へ延び且つ互いに隣接する前記凸部と凸部との間に配設されるよう、前記芯材の両端部が鋼矢板の表面に取り付けられる水中金属構造物の防食電着被膜形成方法。
A substrate adjustment process that removes deposits on the surface of underwater metal structures,
A steel core material in which both ends are connected to the surface of the underwater metal structure on the surface of the underwater metal structure from which deposits have been removed in the substrate adjustment step, and a magnesium alloy coated on the core material. Perform the anode mounting process and mount the anode with
The underwater metal structure is a steel sheet pile that is connected and arranged so that a concave portion and a convex portion are formed.
In the anode mounting step, both ends of the core material are attached to the surface of the steel sheet pile so that the magnesium alloy of the anode extends in the water depth direction and is disposed between the convex portions adjacent to each other. A method for forming an anticorrosion electrodeposition film on an underwater metal structure.
前記陽極取付工程は、
前記鋼矢板の表面に形成すべき電着被膜の必要膜厚tを設定する必要膜厚設定工程と、
該必要膜厚設定工程で設定された必要膜厚tに基づいて単位面積当たりの通電量iを求める単位面積通電量算出工程と、
前記鋼矢板の表面における電着被膜を形成すべき表面積Sを設定する表面積設定工程と、
該表面積設定工程で設定された表面積Sと前記単位面積通電量算出工程で求められた単位面積当たりの通電量iとに基づき必要通電量Iを求める必要通電量算出工程と、
連結配置される前記鋼矢板の凹部の数nを設定する凹部設定工程と、
前記必要通電量算出工程で求められた必要通電量Iと前記凹部設定工程で設定された凹部の数nとに基づき前記鋼矢板の凹部一個当たりの凹部通電量Iを求める凹部通電量算出工程と、
前記陽極の一本当たりの発生電流iを設定する陽極発生電流設定工程と、
前記凹部通電量算出工程で求められた凹部通電量Iと前記陽極発生電流設定工程で設定された発生電流iとに基づき前記鋼矢板の凹部一個に取り付けるべき陽極の本数Yを求める陽極本数設定工程と
を含む請求項記載の水中金属構造物の防食電着被膜形成方法。
The anode mounting step is
The required film thickness setting step for setting the required film thickness t of the electrodeposition film to be formed on the surface of the steel sheet pile, and the required film thickness setting step.
A unit area energization amount calculation step for obtaining an energization amount i per unit area based on the required film thickness t set in the required film thickness setting step, and a unit area energization amount calculation step.
A surface area setting step for setting a surface area S on which an electrodeposition coating is to be formed on the surface of the steel sheet pile, and a surface area setting step.
The required energization amount calculation step of obtaining the required energization amount I based on the surface area S set in the surface area setting step and the energization amount i per unit area obtained in the unit area energization amount calculation step.
A recess setting step for setting the number n of recesses of the steel sheet piles to be connected and arranged, and a recess setting step.
Recessed energization amount calculation step for obtaining the recess energizing amount Io per recess of the steel sheet pile based on the required energizing amount I obtained in the required energizing amount calculation step and the number n of recesses set in the recess setting step. When,
The anode generating current setting step of setting the generated current yy per anode and the anode generating current setting step.
The number of anodes Y to be attached to one recess of the steel sheet pile is obtained based on the recess energization amount Io obtained in the recess energization amount calculation step and the generated current ii set in the anode generation current setting step. The method for forming an anticorrosion electrodeposition film on an underwater metal structure according to claim 1 , which includes a setting step.
前記陽極取付工程で、前記芯材の両端部は、前記鋼矢板の凸部の表面に取り付けられる請求項記載の水中金属構造物の防食電着被膜形成方法。 The method for forming an anticorrosion electrodeposition film on an underwater metal structure according to claim 2 , wherein both ends of the core material are attached to the surface of the convex portion of the steel sheet pile in the anode mounting step. 前記陽極取付工程で、前記芯材の両端部は、前記鋼矢板の凸部の表面に固着されたブラケットに対し締結部材により着脱自在に取り付けられる請求項記載の水中金属構造物の防食電着被膜形成方法。 The anticorrosion electrodeposition of the underwater metal structure according to claim 3 , wherein in the anode mounting step, both ends of the core material are detachably attached to a bracket fixed to the surface of the convex portion of the steel sheet pile by a fastening member. Film forming method.
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