EP1770188A1 - Method of forming anticorrosion coating - Google Patents
Method of forming anticorrosion coating Download PDFInfo
- Publication number
- EP1770188A1 EP1770188A1 EP05736723A EP05736723A EP1770188A1 EP 1770188 A1 EP1770188 A1 EP 1770188A1 EP 05736723 A EP05736723 A EP 05736723A EP 05736723 A EP05736723 A EP 05736723A EP 1770188 A1 EP1770188 A1 EP 1770188A1
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- European Patent Office
- Prior art keywords
- coating
- steel structure
- seawater
- anticorrosive coating
- magnesium hydrate
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- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02D—FOUNDATIONS; EXCAVATIONS; EMBANKMENTS; UNDERGROUND OR UNDERWATER STRUCTURES
- E02D5/00—Bulkheads, piles, or other structural elements specially adapted to foundation engineering
- E02D5/22—Piles
- E02D5/64—Repairing piles
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D9/00—Electrolytic coating other than with metals
- C25D9/04—Electrolytic coating other than with metals with inorganic materials
- C25D9/08—Electrolytic coating other than with metals with inorganic materials by cathodic processes
- C25D9/10—Electrolytic coating other than with metals with inorganic materials by cathodic processes on iron or steel
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F2213/00—Aspects of inhibiting corrosion of metals by anodic or cathodic protection
- C23F2213/30—Anodic or cathodic protection specially adapted for a specific object
- C23F2213/31—Immersed structures, e.g. submarine structures
Definitions
- the present invention relates to a process for forming anticorrosive coating and more specifically to a process for forming anticorrosive coating on a marine steel structure in a short period.
- a process for anticorrosion of a marine steel structure has been proposed in which the steel structure is used as a cathode, an anode being arranged in seawater to be opposed to the steel structure. Direct current is passed between the electrodes to form coating (anticorrosive coating) on the steel structure through electrolytic reaction of the seawater, thereby attaining anticorrosion of the steel structure.
- Reference 1 discloses that a steel member constituting a surface of a marine steel structure is used as a cathode, an anode being arranged in seawater to be opposed to the steel member. Direct current is passed between the electrodes to remove rust and the like scales on the surface of the steel structure. Then, direct current is passed between the electrodes to deposit electrodeposit, which has electrolytic reaction product of the seawater as dominant constituent, on the surface and any corroded pores of the steel structure, thereby forming anticorrosive coating. [Reference 1] JP10-313728A
- the coating formed as mentioned above on the marine steel structure through electrolytic reaction of the seawater has calcium carbonate CaCO 3 and magnesium hydrate Mg(OH) 2 as main components.
- CaCO 3 calcium carbonate formed hard in hardness that exhibits anticorrosive effect. Therefore, in order to make a marine steel structure anticorrosive, anticorrosive coating having calcium carbonate as dominating component must be formed on the steel structure.
- composition ratio of calcium carbonate in the coating is high and that of magnesium hydrate is low.
- composition ratio of calcium carbonate is decreased and that of magnesium hydrate is increased. It is regarded that good anticorrosion property is obtained when coating composition ratio of calcium carbonate to magnesium hydrate is 1 or more.
- the conventional process for forming anticorrosive coating as disclosed in Reference 1 requires long construction period and long-term management and is costly due to increased electric power consumption, so that the process has not been practically applied except special cases such as bridge piers at sites in deep water or in violent tidal current.
- the invention was made in view of the above and has its object to provide a process for forming anticorrosive coating which can be conducted cheaply in a short period, thereby easily leading to general application to marine steel structures.
- the invention is directed to a process for forming anticorrosive coating on a marine steel structure wherein the steel structure is used as a cathode, an anode being arranged in seawater to be opposed to said steel structure, direct current being passed between the electrodes, anticorrosive coating being formed on the steel structure through electrolytic reaction of the seawater, thereby attaining anticorrosion of the marine steel structure, characterized by passing the electric current between the electrodes so as to have current density to form coating having magnesium hydrate as dominant constituent on said marine steel structure, thereby forming the coating with a predetermined thickness, then stopping supply of the electric current to thereby provide anticorrosive coating through compositional substitution effect which occurs in the presence of the seawater to substitute calcium carbonate for the magnesium hydrate.
- the electric current is passed between the electrodes so as to attain current density of the marine steel structure in a range of 3 to 10 A/m 2 .
- a process for forming anticorrosive coating of the invention electric current is passed between electrodes so as to keep high current density of a marine steel structure, so that coating with magnesium hydrate as dominant constituent is formed on the steel structure in a short period. Then, supply of the electric current is stopped to utilize a compositional substitution effect which occurs in the presence of the seawater to substitute calcium carbonate for the magnesium hydrate, thereby forming anticorrosive coating.
- the invention has an effect that it can form good anticorrosive coating with calcium carbonate as dominant constituent in by far a shorter period than ever before.
- the invention has an effect that it can be easily applicable to any kind of marine steel structures unlike the conventional process with limited applicability to special sites.
- Fig. 2 is a side view exemplifying equipment components in application of a process for forming anticorrosive coating according to the invention to a steel caisson of a breakwater which is an example of a marine steel structure; and Fig. 3, a front view looking in the direction of arrows III in Fig. 2.
- reference numeral 1 denotes steel caissons which constitute a breakwater; 2, a DC power supply on arranged for example on a top of the steel caisson 1; and 3, undersea members suspended in seawater to be opposed in a predetermined distance to the submerged surface of the steel caisson 1 and spaced from each other by a predetermined distance and in parallel with the surface of the steel caisson 1.
- the undersea members 3 may be made from soluble material such as magnesium or aluminum or insoluble material such as titanium.
- the DC power supply 2 is connected at its minus (-) side to the steel caisson 1 so as to use the steel caisson 1 as a cathode and is connected at its plus (+) side to the undersea member 3 so as to use the undersea member 3 as an anode.
- Such construction is made to each of the plural steel caissons 1.
- a predetermined constant current is passed between the electrodes, i.e., between the steel caisson 1 and the undersea member 3 by the DC power supply 2, so that deposited coating is formed on the steel caisson 1 through electrolytic reaction of the seawater.
- monitoring electrodes 4 are arranged at plural points on the submerged surface of each steel caisson 1, a monitoring unit 5 being arranged for example on the top of the steel caisson 1 so as to determine and display electric potential from detected values of the respective monitoring electrodes 4.
- the monitoring unit 5 severs for checking that electric current with a predetermined current density is passed through the steel caisson 1 through application of constant electric current on the steel caisson 1 by the DC power supply 2.
- a constant-potential system which keeps constant the electric potential (voltage) of the steel caisson 1.
- the monitoring unit 5 may have the function of a controller for automatically controlling the voltage of the DC power supply 2 so as to keep the detected electric potential to be a predetermined constant potential.
- Fig. 4 shows the fact that, as the current density is increased, the generated amount calcium carbonate is rapidly increased into its peak with the current density being 0.5 A/m 2 or so; as the current density is further increased, then the generated amount of calcium carbonate tends to be rapidly decreased.
- Fig. 5 shows the fact that, as the current density is increased up to about 7A/m 2 , the generated amount of magnesium hydrate is increased toward its peak; as the current density is further increased, then the generated amount of magnesium hydrate tends to be decreased.
- Fig. 5 The data shown in Fig. 5 are those in laboratory experiment with still water condition, so that in actual sea areas, electrodeposition efficiency may be lowered due to effect of tidal current (see, for example, Honshi-Giho Vol. 24, No. 95 (Dec. 2000 )) .
- tidal current see, for example, Honshi-Giho Vol. 24, No. 95 (Dec. 2000 )
- tests were conducted with respect to generated amount of coating in real sea areas to find out that an optimum range of current density in real sea areas is 3 to 10 A/m 2 .
- the coating formed on the steel caisson 1 has magnesium hydrate as dominant constituent (for example, 95% of magnesium hydrate), failing to be anticorrosive coating.
- the inventors made researches so as to change the coating with magnesium hydrate as dominant constituent and formed in a short period as mentioned above into anticorrosive coating with calcium carbonate as dominant constituent and found out that compositional substitution effect occurs in seawater to substitute calcium carbonate for the magnesium hydrate, thereby utilizing such effect to attain formation of anticorrosive coating.
- the inventors used experimental equipment similar to that shown in Figs. 2 and 3 to conduct tests for forming coating so as to ascertain the above-mentioned compositional substitution effect.
- cathode substrate in opposed relationship to the steel caisson 1 is made from SS(stainless steel)400 and the anode member corresponding to the undersea member 3 is made from Mg, using natural seawater with temperature of 25°C with the current applying condition of current density being 3 A/m 2 .
- coating test for 30 hours was conducted.
- thickness L of the coating 7 generated on the cathode substrate 6 in the test was detected to be 105 ⁇ m.
- the composition obtained in chemical analysis of the coating 7 was, as shown in Fig. 8, about 5% of calcium carbonate and about 95% of magnesium hydrate, most of the composition being magnesium hydrate.
- reaction formula (1) occurs to bring about the reaction formula (2), leading to the reaction formula (3).
- Mg(OH) 2 ⁇ Mg 2+ + 2OH - (1) Ca 2+ + H 2 CO 3 + 2OH - ⁇ CaCO 3 + 2H 2 O (2)
- the coating 7 with magnesium hydrate as dominant constituent as shown in Fig. 6 is replaced by calcium carbonate through the above-mentioned compositional substitution effect to thereby form, as shown in Fig. 7, the hard anticorrosive coating having calcium carbonate as dominant constituent with no substantial change in thickness L.
- the electric current applying condition was the current density of 3 A/m 2 . That is, the experiments were conducted with lower current density since the coating tends to fall off in the case of the experimental equipment with no flows of seawater. However, it turned out that in actual natural seawater with flows, coating can be formed well with no falling-off even if the process is conducted with the current density of as high as 3 to 10 A/m 2 .
- anticorrosive coating according to the invention can be formed in a very short period on the order of one month or one month and a half. This facilitates the process management and brings about reduction in electricity consumption, resulting in decrease in cost. Therefore, with no limitation to the special sites unlike the conventional process, the invention can be easily applied to any kinds of marine steel structures.
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- Materials Engineering (AREA)
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- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mining & Mineral Resources (AREA)
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Abstract
Description
- The present invention relates to a process for forming anticorrosive coating and more specifically to a process for forming anticorrosive coating on a marine steel structure in a short period.
- A process for anticorrosion of a marine steel structure has been proposed in which the steel structure is used as a cathode, an anode being arranged in seawater to be opposed to the steel structure. Direct current is passed between the electrodes to form coating (anticorrosive coating) on the steel structure through electrolytic reaction of the seawater, thereby attaining anticorrosion of the steel structure.
- Thus,
Reference 1 discloses that a steel member constituting a surface of a marine steel structure is used as a cathode, an anode being arranged in seawater to be opposed to the steel member. Direct current is passed between the electrodes to remove rust and the like scales on the surface of the steel structure. Then, direct current is passed between the electrodes to deposit electrodeposit, which has electrolytic reaction product of the seawater as dominant constituent, on the surface and any corroded pores of the steel structure, thereby forming anticorrosive coating.
[Reference 1]JP10-313728A - The coating formed as mentioned above on the marine steel structure through electrolytic reaction of the seawater has calcium carbonate CaCO3 and magnesium hydrate Mg(OH)2 as main components. As is known in the art, it is calcium carbonate formed hard in hardness that exhibits anticorrosive effect. Therefore, in order to make a marine steel structure anticorrosive, anticorrosive coating having calcium carbonate as dominating component must be formed on the steel structure.
- As disclosed also in
Reference 1, relationship between coating composition on a marine steel structure and current density due to electric current applied between electrodes is as shown in Fig. 1. More specifically, in a condition of low current density, composition ratio of calcium carbonate in the coating is high and that of magnesium hydrate is low. As the current density is elevated, composition ratio of calcium carbonate is decreased and that of magnesium hydrate is increased. It is regarded that good anticorrosion property is obtained when coating composition ratio of calcium carbonate to magnesium hydrate is 1 or more. - So, it is disclosed in
Reference 1 that current density during electrodeposition is selected within a range, of 0.2 to 2 A/m2 (1 A/m2 on an average) so as to form anticorrosive coating with calcium carbonate as dominant constituent and that anticorrosive coating in the form of hard electrodeposition coating and with thickness of about 5 mm or more is formed on the marine steel structure. - However, it is known that a long period of about 10 months or more is required for formation of anticorrosive coating with calcium carbonate as dominant constituent and having thickness of for example 5 mm or more by a low current density of for example 1 A/m2 as disclosed in
Reference 1. - Thus, the conventional process for forming anticorrosive coating as disclosed in
Reference 1 requires long construction period and long-term management and is costly due to increased electric power consumption, so that the process has not been practically applied except special cases such as bridge piers at sites in deep water or in violent tidal current. - The invention was made in view of the above and has its object to provide a process for forming anticorrosive coating which can be conducted cheaply in a short period, thereby easily leading to general application to marine steel structures.
- The invention is directed to a process for forming anticorrosive coating on a marine steel structure wherein the steel structure is used as a cathode, an anode being arranged in seawater to be opposed to said steel structure, direct current being passed between the electrodes, anticorrosive coating being formed on the steel structure through electrolytic reaction of the seawater, thereby attaining anticorrosion of the marine steel structure, characterized by passing the electric current between the electrodes so as to have current density to form coating having magnesium hydrate as dominant constituent on said marine steel structure, thereby forming the coating with a predetermined thickness, then stopping supply of the electric current to thereby provide anticorrosive coating through compositional substitution effect which occurs in the presence of the seawater to substitute calcium carbonate for the magnesium hydrate.
- It is preferable in the above-mentioned invention that the electric current is passed between the electrodes so as to attain current density of the marine steel structure in a range of 3 to 10 A/m2.
- According to a process for forming anticorrosive coating of the invention, electric current is passed between electrodes so as to keep high current density of a marine steel structure, so that coating with magnesium hydrate as dominant constituent is formed on the steel structure in a short period. Then, supply of the electric current is stopped to utilize a compositional substitution effect which occurs in the presence of the seawater to substitute calcium carbonate for the magnesium hydrate, thereby forming anticorrosive coating. As a result, the invention has an effect that it can form good anticorrosive coating with calcium carbonate as dominant constituent in by far a shorter period than ever before.
- Such formation of anticorrosive coating in a short period leads to reduction in construction period and easiness in management as well as reduction in cost due to reduced electric power consumption. Therefore, the invention has an effect that it can be easily applicable to any kind of marine steel structures unlike the conventional process with limited applicability to special sites.
-
- [Fig. 1] A diagram showing relationship between coating composition on a marine steel structure and current density due to electric current applied between electrodes.
- [Fig. 2] A side view exemplifying equipment components in application of a process for forming anticorrosive coating according to the invention to a steel caisson of a breakwater which is an example of a marine steel structure.
- [Fig. 3] A front view looking in the direction of arrows III in Fig. 2.
- [Fig. 4] A diagram showing test results of generated amount of calcium carbonate.
- [Fig. 5] A diagram showing test results of generated amount of magnesium hydrate.
- [Fig. 6] A view showing coating generated on a cathode substrate in the test equipment.
- [Fig. 7] A view showing change of the coating in Fig. 5 into anticorrosive coating through compositional substitution effect.
- [Fig. 8] A diagram showing variation in composition ratio of magnesium hydrate and calcium carbonate by stopping supply of electric current after formation of coating with magnesium hydrate as dominant constituent.
- [Fig. 9] A diagram showing variation of the coating amount on a mol basis.
- [Fig. 10] A diagram showing variation of the coating amount on a weight basis.
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- 1
- steel caisson (marine steel structure)(cathode)
- 2
- DC power supply
- 3
- undersea member (anode)
- 7
- coating
- 8
- anticorrosive coating
- An embodiment of the invention will be described in conjunction with the attached drawings.
- Fig. 2 is a side view exemplifying equipment components in application of a process for forming anticorrosive coating according to the invention to a steel caisson of a breakwater which is an example of a marine steel structure; and Fig. 3, a front view looking in the direction of arrows III in Fig. 2. In the figures,
reference numeral 1 denotes steel caissons which constitute a breakwater; 2, a DC power supply on arranged for example on a top of thesteel caisson 1; and 3, undersea members suspended in seawater to be opposed in a predetermined distance to the submerged surface of thesteel caisson 1 and spaced from each other by a predetermined distance and in parallel with the surface of thesteel caisson 1. Theundersea members 3 may be made from soluble material such as magnesium or aluminum or insoluble material such as titanium. - The
DC power supply 2 is connected at its minus (-) side to thesteel caisson 1 so as to use thesteel caisson 1 as a cathode and is connected at its plus (+) side to theundersea member 3 so as to use theundersea member 3 as an anode. Such construction is made to each of theplural steel caissons 1. - A predetermined constant current is passed between the electrodes, i.e., between the
steel caisson 1 and theundersea member 3 by theDC power supply 2, so that deposited coating is formed on thesteel caisson 1 through electrolytic reaction of the seawater. - Moreover, as shown in Fig. 3, monitoring
electrodes 4 are arranged at plural points on the submerged surface of eachsteel caisson 1, amonitoring unit 5 being arranged for example on the top of thesteel caisson 1 so as to determine and display electric potential from detected values of therespective monitoring electrodes 4. Themonitoring unit 5 severs for checking that electric current with a predetermined current density is passed through thesteel caisson 1 through application of constant electric current on thesteel caisson 1 by theDC power supply 2. At sites with great tidal variation where an area of a submerged surface on thesteel caisson 1 varies greatly to greatly change the current density of the electric current passed through thesteel caisson 1, there may be employed a constant-potential system which keeps constant the electric potential (voltage) of thesteel caisson 1. In this case, themonitoring unit 5 may have the function of a controller for automatically controlling the voltage of theDC power supply 2 so as to keep the detected electric potential to be a predetermined constant potential. - Mode of operation of the invention will be described in conjunction with experimental example.
- Using the equipment shown in Figs. 2 and 3, the inventors tested generated amounts of calcium carbonate and magnesium hydrate, respectively, when the current density passed through the
steel caisson 1 is gradually varied with the current-carrying capacity through theDC power supply 2 being constant or 60A·h/m2. The test results of the generated amounts of calcium carbonate and magnesium hydrate are shown in Fig. 4 and in Fig. 5, respectively. - Fig. 4 shows the fact that, as the current density is increased, the generated amount calcium carbonate is rapidly increased into its peak with the current density being 0.5 A/m2 or so; as the current density is further increased, then the generated amount of calcium carbonate tends to be rapidly decreased.
- Fig. 5 shows the fact that, as the current density is increased up to about 7A/m2, the generated amount of magnesium hydrate is increased toward its peak; as the current density is further increased, then the generated amount of magnesium hydrate tends to be decreased.
- It turned out that the above-mentioned tendencies in Figs. 4 and 5 coincide with the conventionally known relationship between current density and coating shown in Fig. 1.
- Then, the inventors took notice of Fig. 5 to find out that with the current density being set to be as high as of 3 to 7 A/m2, generating speed of coating can be substantially increased, so that coating with intended thickness can be formed in a short period. The data shown in Fig. 5 are those in laboratory experiment with still water condition, so that in actual sea areas, electrodeposition efficiency may be lowered due to effect of tidal current (see, for example, Honshi-Giho Vol. 24, No. 95 (Dec. 2000)) . As a result, tests were conducted with respect to generated amount of coating in real sea areas to find out that an optimum range of current density in real sea areas is 3 to 10 A/m2.
- However, with the current density being set to be as high as 3 to 10 A/m2 as mentioned above, the coating formed on the
steel caisson 1 has magnesium hydrate as dominant constituent (for example, 95% of magnesium hydrate), failing to be anticorrosive coating. - Thus, the inventors made researches so as to change the coating with magnesium hydrate as dominant constituent and formed in a short period as mentioned above into anticorrosive coating with calcium carbonate as dominant constituent and found out that compositional substitution effect occurs in seawater to substitute calcium carbonate for the magnesium hydrate, thereby utilizing such effect to attain formation of anticorrosive coating.
- The inventors used experimental equipment similar to that shown in Figs. 2 and 3 to conduct tests for forming coating so as to ascertain the above-mentioned compositional substitution effect.
- In the experimental equipment, cathode substrate in opposed relationship to the
steel caisson 1 is made from SS(stainless steel)400 and the anode member corresponding to theundersea member 3 is made from Mg, using natural seawater with temperature of 25°C with the current applying condition of current density being 3 A/m2. Thus, coating test for 30 hours was conducted. - As shown in Fig. 6 with no submerged period, thickness L of the
coating 7 generated on thecathode substrate 6 in the test was detected to be 105µm. The composition obtained in chemical analysis of thecoating 7 was, as shown in Fig. 8, about 5% of calcium carbonate and about 95% of magnesium hydrate, most of the composition being magnesium hydrate. - Then, tests were conducted to ascertain the compositional substitution effect by the
coating 7 with magnesium hydrate as dominant constituent as mentioned above. - More specifically, after the
coating 7 with magnesium hydrate as dominant constituent as mentioned above was formed on thecathode substrate 6, supply of electric current by the DC power supply was stopped. Thereafter, the coating was kept submerged in seawater; coating composition ratio of magnesium hydrate and calcium carbonate and coating amounts in g/cm2 and in mmol thereof were detected at 7, 14 and 21 days after the start of submerging (the stop of current supply). - According to Fig. 8, as the submerging was started, the dominant magnesium hydrate was decreased and calcium carbonate was increased; it turned out that dominance in composition ratio between magnesium hydrate and calcium carbonate was reversed substantially at 17 days after the submerging.
- With the lapse of submerged period, there was no variation in coating amount on the mol basis as shown in Fig. 9. On the other hand, there appeared slight increase tendency in coating amount on the weight basis as shown in Fig. 10. This tendency means change of the coating composition ratio due to decrease of magnesium hydrate and substitutive increase of calcium carbonate with the lapse of submerged period as shown in Fig. 8. More specifically, change of the coating composition ratio with no change of the total amount on the mol basis as shown in Fig. 9 is regarded to mean that dissolution and deposition reactions of magnesium hydrate and calcium carbonate, respectively, in the coating concurrently occurred with chemical equivalent of substantially 1:1. As a result, coating amount on the weight basis was increased as shown in Fig. 10 since calcium carbonate with higher molar weight (Mw = 100) was substituted for the magnesium hydrate with lower molar weight (Mw = 58).
- More specifically, it is regarded that the following reaction formula (1) occurs to bring about the reaction formula (2), leading to the reaction formula (3).
Mg(OH)2 → Mg2+ + 2OH- (1)
Ca2+ + H2CO3 + 2OH- → CaCO3 + 2H2O (2)
Mg(OH)2 + Ca2+ + H2CO3→Mg2+ + CaCO3 + 2H2O (3)
- Thus, the
coating 7 with magnesium hydrate as dominant constituent as shown in Fig. 6 is replaced by calcium carbonate through the above-mentioned compositional substitution effect to thereby form, as shown in Fig. 7, the hard anticorrosive coating having calcium carbonate as dominant constituent with no substantial change in thickness L. - As can be seen from Fig. 8, submerging of 17 days or more brings about excellent
anticorrosive coating 8 with coating composition ratio of calcium carbonate to magnesium hydrate being 1 or more. - In the experimental tests shown in the above, the electric current applying condition was the current density of 3 A/m2. That is, the experiments were conducted with lower current density since the coating tends to fall off in the case of the experimental equipment with no flows of seawater. However, it turned out that in actual natural seawater with flows, coating can be formed well with no falling-off even if the process is conducted with the current density of as high as 3 to 10 A/m2.
- Thus, by contrast with the conventional process having a period of 10 months or more in formation of anticorrosive coating, anticorrosive coating according to the invention can be formed in a very short period on the order of one month or one month and a half. This facilitates the process management and brings about reduction in electricity consumption, resulting in decrease in cost. Therefore, with no limitation to the special sites unlike the conventional process, the invention can be easily applied to any kinds of marine steel structures.
- When a process for forming anticorrosive coating according to the invention is applied to an existing marine steel structure and where any extraneous matter such as rust on a surface of the marine steel structure is required to be removed beforehand, various countermeasures may be employed such as application of direct current between electrodes for removal of rust and the like, removal through injection of high-pressure water or removal through manpower.
- It is to be understood that the invention is not limited to the above embodiment ahd that various changes and modifications may be made without departing from the scope of the invention. For example, the description of the embodiment has been made with respect to steel caisson as an example; however, the invention may be similarly applicable for anticorrosion of various marine steel structures such as steel sheet pile or steel bridge pier.
Claims (2)
- A process for forming anticorrosive coating on a marine steel structure wherein the steel structure (1) is used as a cathode, an anode (3) being arranged in seawater to be opposed to said steel structure (1), direct current being passed between the electrodes (1 and 3), anticorrosive coating (8) being formed on the steel structure (1) through electrolytic reaction of the seawater, thereby attaining anticorrosion of the marine steel structure (1), characterized by passing the electric current between the electrodes (1 and 3) so as to have current density to form coating (7) having magnesium hydrate as dominant constituent on said marine steel structure (1), thereby forming the coating (7) with a predetermined thickness, then stopping supply of the electric current to thereby provide anticorrosive coating (7) through compositional substitution effect which occurs in the presence of the seawater to substitute calcium carbonate for the magnesium hydrate.
- A process for forming anticorrosive coating as claimed in claim 1, characterized in that the electric current is passed between the electrodes (1 and 3) so as to attain current density of the marine steel structure (1) in a range of 3 to 10 A/m2.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004140715A JP4424059B2 (en) | 2004-05-11 | 2004-05-11 | Method for forming anticorrosion film |
| PCT/JP2005/008133 WO2005108645A1 (en) | 2004-05-11 | 2005-04-28 | Method of forming anticorrosion coating |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1770188A1 true EP1770188A1 (en) | 2007-04-04 |
| EP1770188A4 EP1770188A4 (en) | 2008-07-23 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP05736723A Withdrawn EP1770188A4 (en) | 2004-05-11 | 2005-04-28 | Method of forming anticorrosion coating |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20080029401A1 (en) |
| EP (1) | EP1770188A4 (en) |
| JP (1) | JP4424059B2 (en) |
| NO (1) | NO20065301L (en) |
| WO (1) | WO2005108645A1 (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4217245B2 (en) | 2006-01-20 | 2009-01-28 | 株式会社神戸製鋼所 | High strength steel with excellent hydrogen embrittlement resistance |
| JP5434237B2 (en) * | 2009-04-28 | 2014-03-05 | 株式会社Ihi | Method and apparatus for maintaining anticorrosive deposition film |
| JP5387280B2 (en) * | 2009-09-25 | 2014-01-15 | 株式会社Ihi | Electrodeposition coating device |
| JP5387356B2 (en) * | 2009-11-24 | 2014-01-15 | 株式会社Ihi | Corrosion-proof electrodeposition coating method and apparatus for marine steel structures |
| JP5740845B2 (en) * | 2010-06-01 | 2015-07-01 | 株式会社Ihi | Anti-corrosion method for offshore steel structures |
| JP5740851B2 (en) * | 2010-06-23 | 2015-07-01 | 株式会社Ihi | Steel sheet pile electrodeposition protection system |
| JP5678505B2 (en) * | 2010-07-26 | 2015-03-04 | 株式会社Ihi | Method of forming anti-corrosion coating for offshore steel structures in tidal currents |
| FR3031347B1 (en) * | 2015-01-06 | 2017-07-21 | Electricite De France | CATHODIC PROTECTION OF A HOLLOW METAL STRUCTURE AGAINST CORROSION |
| JP7066465B2 (en) * | 2018-03-20 | 2022-05-13 | 株式会社Ihi | Method for forming anticorrosion electrodeposition coating on underwater metal structures |
| CN118997134A (en) * | 2024-08-13 | 2024-11-22 | 广州航海学院 | Repairing method for steel pipe pile of port and wharf |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4246075A (en) * | 1979-03-19 | 1981-01-20 | Marine Resources Company | Mineral accretion of large surface structures, building components and elements |
| JPS61261499A (en) * | 1985-05-13 | 1986-11-19 | Mitsui Eng & Shipbuild Co Ltd | Electrodeposition device |
| JP3000411B2 (en) * | 1992-08-19 | 2000-01-17 | 三井造船株式会社 | Early diagnosis method and repair method for cracks in reinforced concrete structures |
| JPH10313728A (en) * | 1997-05-20 | 1998-12-02 | Honsyu Shikoku Renrakukiyou Kodan | Corrosion protection of marine steel structures |
| JP4126513B2 (en) * | 1998-08-19 | 2008-07-30 | 株式会社Ihi | Antifouling method and antifouling device by electrocoating |
| JP4131055B2 (en) * | 1999-06-04 | 2008-08-13 | 株式会社Ihi | Anti-fouling method for wire mesh by electro-coating |
| KR100539239B1 (en) * | 2003-06-25 | 2005-12-27 | 삼성전자주식회사 | Plating method for preventing failure due to plating-stop and plating apparatus therefor |
-
2004
- 2004-05-11 JP JP2004140715A patent/JP4424059B2/en not_active Expired - Fee Related
-
2005
- 2005-04-28 US US11/547,475 patent/US20080029401A1/en not_active Abandoned
- 2005-04-28 EP EP05736723A patent/EP1770188A4/en not_active Withdrawn
- 2005-04-28 WO PCT/JP2005/008133 patent/WO2005108645A1/en not_active Ceased
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2006
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Also Published As
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|---|---|
| JP2005320602A (en) | 2005-11-17 |
| WO2005108645A1 (en) | 2005-11-17 |
| EP1770188A4 (en) | 2008-07-23 |
| US20080029401A1 (en) | 2008-02-07 |
| NO20065301L (en) | 2006-11-17 |
| JP4424059B2 (en) | 2010-03-03 |
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