WO2005014890A1 - Solution electrolytique - Google Patents

Solution electrolytique Download PDF

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Publication number
WO2005014890A1
WO2005014890A1 PCT/GB2003/003160 GB0303160W WO2005014890A1 WO 2005014890 A1 WO2005014890 A1 WO 2005014890A1 GB 0303160 W GB0303160 W GB 0303160W WO 2005014890 A1 WO2005014890 A1 WO 2005014890A1
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Prior art keywords
metal ion
electrolyte solution
solution according
coating
transition metal
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PCT/GB2003/003160
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English (en)
Inventor
Kevin Richard Baldwin
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SEAMLESS PLATING (UK) Ltd
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SEAMLESS PLATING (UK) Ltd
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Priority to PCT/GB2003/003160 priority Critical patent/WO2005014890A1/fr
Priority to AU2003254474A priority patent/AU2003254474A1/en
Publication of WO2005014890A1 publication Critical patent/WO2005014890A1/fr
Anticipated expiration legal-status Critical
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    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/48—After-treatment of electroplated surfaces
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10—Electroplating with more than one layer of the same or of different metals
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/627—Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance

Definitions

  • the present invention relates to an electrolyte solution and process that furnishes passivated metal coatings to substrate materials, and to articles treated using the same solution and process.
  • Electroplating solutions and processes are extensively employed to electrodeposit metallic coatings to substrates such as steels. Such coatings are used to afford desirable properties to the substrate material; for example, corrosion resistance, decorative finish, or wear resistance.
  • Established metallic coatings include cadmium, chromium, cobalt, copper, nickel, tin, silver, and gold.
  • Other known coatings include iron, manganese, platinum, rhodium, and indium. Where sacrificial corrosion resistance is required, zinc is often the preferred choice.
  • Zinc can be electrodeposited either alone, or in combination with other metals to form alloy coatings, for example, zinc-cobalt alloys, zinc-iron alloys, and zinc- nickel alloys.
  • Electrolytes currently used for plating purposes comprise various chemical species that serve one or more of the following functions : to provide a source of the metal or metals being deposited, to form complexes with ions of the depositing metal, to provide conductivity, to stabilise the solution e.g. against hydrolysis, to act as a buffer, to modify or regulate the physical form of the deposit, to aid in dissolving anodes, or to modify specific properties either of the solution or the deposit.
  • a typical electrolyte used to deposit zinc might comprise zinc chloride as the source of the metal ions, ammonium chloride to provide conductivity, a buffer such as boric acid .to regulate acidity, a detergent to prevent pores from forming in the deposit, and organic agents such as chlorobenzaldehyde to encourage the formation of bright and reflective coatings.
  • Other additives known as levelling agents, may be employed to promote the formation of flat electrodeposits that are free of dendrites .
  • levelling agents may be employed to promote the formation of flat electrodeposits that are free of dendrites .
  • zinc electrolyte including alkaline solutions that use cyanide salts for conductivity, and alkaline solutions that are free of cyanides.
  • Acidic zinc electrolytes may also contain nickel, cobalt, iron, or tin salts. These metals are often added as chlorides or sulphates. Such electrolytes are routinely used to deposit alloy coatings, namely, zinc- nickel alloys, zinc-cobalt alloys, zinc-iron alloys or zinc-tin alloys . These are more corrosion resistant than zinc alone. Alkaline solutions can also be used to produce similar alloy coatings provided complexing agents are added to the electrolytes partly in order to maintain " selected metal ions in solution. Other metals such as tin and copper can be alloyed with dissimilar metals using the same principles. Examples include tin-lead, tin- bismuth, tin-nickel, copper-zinc, and copper-tin.
  • An electroplating cell comprises the electrolyte, an anode material, and the article to be plated, which is the cathode.
  • the anode and cathode are connected to an external power supply, and electricity is passed through the cell.
  • the metal ions in the electrolyte are reduced at the cathode to form the desired metal coating.
  • Electroplating cells include vats, barrels, or those employed for continuous strip plating. Commercial electrolytes are supplied with detailed instructions on their preparation and use, and the recommended type of plating equipment.
  • the electrodeposited coating does not possess the range of properties required for the intended application.
  • their electrodeposited zinc coatings tend to react with moisture in the air and . forms loose corrosion products that are unsightly and prevent the adhesion of paints.
  • the coatings are also insufficiently decorative or lack adequate corrosion resistance.
  • These problems are also encountered with other deposits such as the range of zinc, alloys, and a variety of other metal coatings.
  • the above problems are usually overcome through the application of a chromate passivation film.
  • the freshly deposited and rinsed coating may first be treated in several other solutions, such as an acid solution, rinsed again, and then immersed or otherwise brought into a solution of hexavalent chromate.
  • Chromate passivation films impart many beneficial properties, including a decorative finish, additional corrosion resistance, and provide an excellent surface for paints. Chromates can also provide a range of coloured finishes to sometimes quite dull and unattractive coatings, including iridescent, yellow, green, blue, olive drab, and black. They also remove hazes and polish the coating surface to a bright and reflective finish. Chromate passivation films are commercially and routinely applied to a wide range of electrodeposited coatings, including aluminium, cadmium, copper, tin, zinc, and a wide range of alloy coatings, including the range of zinc alloys. Chromates have been in use for over sixty years and extensive ranges of proprietary formulations are commercially available.
  • the article is rinsed several times in water to remove all traces of hexavalent chromium, and the treatment process is concluded by drying the article, often in a stream of warm air.
  • the electroplating of an article followed by the application of a chromate , ⁇ assivation film is an established practice in the art, there are however inherent drawbacks with this practice.
  • the rinse water used to rinse the article following electroplating becomes contaminated with the electrolyte and eventually requires treatment.
  • the rinse water becomes contaminated with cyanide.
  • the cyanide then requires reduction through chemical additions, which produce a precipitate, followed by filtration to remove the solid matter, and subsequent disposal, often to a landfill site.
  • the water left over from this treatment process may require subsequent treatment, for example, through the use of ion exchange columns , to render the water sufficiently pure for reuse or disposal.
  • the chromate contaminated rinse water is treated in several different ways.
  • One approach is to make chemical additions to convert the hexavalent chromium to the less harmful trivalent chromium.
  • a precipitate of the trivalent chromium is produced that is then filtered into a solid cake before disposal tp landfill.
  • the water left over may be evaporated in concrete trenches or subject to further treatment to remove the remaining traces of chromate, for example, by ion exchange chromatography.
  • the treated water may then be reused or sent to drain.
  • the ion exchange columns need periodic regeneration, and the chromium-contaminated resins require . additional special treatment.
  • a first aspect of the present invention is directed to an electrolyte solution comprising at least one plateable metal ion capable of being reduced to the metallic form, at least one transition metal ion species, and a solvent, in which a passivated coating of the at least one plateable metal ion can be deposited on an article.
  • 'plateable metal ion' refers to those metals widely known in the art that are capable of being reduced from their ionic form to their metallic form, ' " usually on the passage of electrical current.
  • the electrodeposited coatings produced by the present invention are more corrosion resistant that those produced conventionally, and, since the passivation films are formed/ without the electrodeposit being exposed to the atmosphere, they are bonded into the- coating at a molecular level, . giving excellent properties such as adhesion, and the aforementioned corrosion resistance.
  • another feature is the capability to produce multi-layer coatings comprising alternate layers of electrodeposited coating and passivation film, which are coatings that cannot be produced by previously proposed methods .
  • the at least one plateable metal ion is selected from: Au + , Au 3+ , Bi 3+ Cd 2+ , Co 2+ , Cr 3+ , Cr 6+ , Cu 2+ , Fe 2+ , Fe 3+ , In + , In 3+ , Mn 2+ , Mn 3+ , Mn 4+ , Ni 2+ , Pb 2+ , Pb 4+ , Pd 2+ , Pt 2+ , Rh 2+ , Rh 3+ , Sn 2+ , Sn 3+ , Sn 4+ , Sb 3+ , Sb + , Sb 5+ ,
  • the at least one plateable metal ion is selected from: Ag + , Co 2+ , Cu + , Cu 2+ , Fe 2+ , Fe 3+ , Mn 2+ , Mn 3+ , Mn 4+ , Ni 2+ , Sn 2+ , Zn 2+ .
  • the counter ion to the at least one plateable metal ion may comprise any ion that gives rise to a salt of sufficient solubility in the chosen solvent.
  • the concentration of the salt or salts comprising the at least one plateable metal will preferably be in a range of 0.1 to 500g/L however higher or lower concentrations than this range may also be used as " required.
  • the at least one transition metal ion complex species is formed from reaction in solution between at least one transition metal ion species and at least one film forming agent.
  • the at least one transition metal ion species is a suitable spec4.es of at least one metal from the transition metal block of the periodic table.
  • the at least one transition metal ion species is chosen from: Ti 2+ , Ti 3+ , Ti 4+ , V + , V 4+ , V + , V 2+ ,
  • the at least one transition metal ion species is an oxide or halide moiety of the at least one transition metal ion species, chosen from: Ti0 3 2 ⁇ , 1_ _ . _ fi_ _ . _ fi_ _ . _ 7- _ . _ ⁇ >.-. _ , _ ?_ _ . _ 1 ?_
  • Ti 3 ClA Ti0 5 6 ⁇ , Ti 2 0 7 6' ' , Ti 6 0 13 2 -, TiF 6 2 ⁇ , Ti; 3 ⁇ 7 2 N Ti 5 0 16 12 N Zr0 3 2" , ZZrr .
  • the at least one transition metal ion species is an oxide moiety of the at least one transition metal ion species, chosen from: V0 3 ⁇ , V ⁇ 4 3 ⁇ , Mo0 4 2 ⁇ , 0 4 2 ⁇ , Mn0 4 ⁇ .
  • Mo0 2 and W0 4 2 ⁇ are employed in the same solution.
  • the Mo0 4 2- concentration is in the range 0.2 to 0.4g/L and the W0 2_ concentration is in the range 0.8 to 1.2g/L.
  • the Mo0 2 ⁇ concentration is 0.2g/L and the W0 4 2_ concentration is 0.8g/L.
  • the counter ion to the at least one transition metal ion species may comprise any cation that gives rise to a sufficiently soluble salt.
  • Trace amounts of the salt or salts comprising the at least one transition metal ion species may be suitable.
  • the concentration range of the salt or salts comprising the at least one transition metal .ion species is 0.01 to lOOg/L, and especially the range is 0.1 to lOg/L. However, concentrations outside these ranges may also be suitable as required.
  • the at least one film forming agent is a species that is capable of reacting with the at least one transition metal ion -species to form a complex of the at least one transition metal ion species such that the complex is furnished with film forming properties.
  • the at least one film forming agent is chosen from: C10 4 ⁇ , Cl 2 0 2 2 ⁇ , N0 2 ⁇ , N0 3 ⁇ , P0 4 3" , S0 3 2" , S 4 0 6 2” , I0 3 " , I0 4 " , 02 2 -, ( OOH ) N (H200H) + , P 2 0 8 4 ⁇ , S 2 0 6 2_ , S 2 0 8 2 N C 2 0 4 2_ , ascorbic acid, tartaric acid or salicyclic acid.
  • the at least one film forming agent is chosen from: S 2 0 8 2" 0 2 2 ⁇ , I0 3 ⁇ .
  • the counter ion to the at least one film " forming agent may comprise any cation that gives rise to a sufficiently soluble salt.
  • the concentration range of the salt or salts comprising the at least one transition metal ion species is 0.01 to lOOOg/L, and especially the range is 0.8 to lOg/L. However, concentrations outside, these ranges may also be suitable as required.
  • the solvent is acidic, neutral, or alkaline
  • the solvent is water
  • the solution further comprises a surfactant.
  • the surfactant minimises pore formation during electroplating. Suitable examples are known in the art and include sodium lauryl sulphate.
  • the solution further comprises a conductivity salt.
  • the salt should provide satisfactory conductivity.
  • suitable salts include ammonium chloride, sodium chloride, aluminium sulphate, and sodium hydroxide, others will readily occur to a man skilled in the art.
  • the solution further comprises a buffer.
  • the buffer should stabilise the solution pH.
  • An example of a buffer is boric acid, other suitable compounds will readily occur to a man skilled in the art.
  • the solution further comprises a levelling agent.
  • the levelling, agent should promote the formation of deposits with even thickness.
  • Suitable salts will be known to those skilled in the art.
  • Examples of levelling agents include liquorice, glucose, saccharin, and ascorbic acid, other suitable compounds will readily occur to a man skilled in the art.
  • the solution further comprises a brightening agent.
  • the chemical passivation films provide the coatings deposited using the solution and process with a bright, reflective, and smooth finish. In some instances, however, it may be desirable to further improve brightness. Suitable brightening additives will be known to those skilled in the art.
  • the solution further comprises a complexing agent.
  • the complexing agent typically maintains the at least one plateable metal ion in acidic or alkaline solutions. Suitable complexing agents will be known to those skilled in the art.
  • the electrolyte solution according to the present invention is suitable for carrying out repeated " electroplating operations. Chemical addition make-up is conducted in accordance with standard procedures, as will be known to those skilled in the art.
  • the process of the present invention is suitable for use with any form of electroplating equipment, for example, vats, barrels, selective plating,- or continuous strip plating.
  • the process for the present invention incorporates solution agitation.
  • the process for the present invention incorporates cathode movement.
  • the process for the present invention incorporates both solution agitation and cathode movement .
  • Figure 1 shows a schematic diagram of a conventional plating process, and a schematic diagram of a passivated coating formed using the process;
  • Figure 2 shows a schematic diagram of a process according to the present invention, and a schematic diagram of the formation of a passivated coating using the process;
  • Figure 3 shows a current-time profile suitable for use in " the process of the present invention to form a coating of the type shown in Fig. 2;
  • Figure 4 shows a current-time profile suitable for use in the process of the present invention to form a multi-layer coating, and a schematic of the • formation of a multi-layer coating according to the process
  • Figure 5 shows a current-time profile of a process according to the present invention and schematic diagrams of a passivated coating formed using the process
  • Figure 6 shows a suitable arrangement for solution agitation according to the present invention.
  • Figure 1 shows a conventional plating process with each box representing a separate stage wherein cleaned articles 2 are typically immersed in the electroplating solution 1 and the desired coating 3 is deposited onto the article from the plating solution.
  • the coated article is then moved through a sequence of rinsing and treatment stages 4 producing rinse water contaminated with plating solution, acid residues, and other many other different chemical species as waste that requires careful handling and treatment.
  • the coated article is transferred to the hexavalent chromate bath. This produces a chromate passivation film on the electrodeposited coating layer 5. Further rinsing concludes the treatment process and generates chromate- " contaminated wastewater, which then requires extensive and expensive treatment.
  • Figure 2 shows a process in accordance with the present' invention.
  • the cleaned article 2 is transferred into the solution 6 and the electrodeposition and chemical passivation stages are carried out from the same solution 6.
  • The- article is thus furnished with both the coating layer 7 and passivation film 8 in a single treatment.
  • the coated and passivated article is then rinsed in water to remove residual amounts of the solution.
  • the rinse water contains "no dangerous or toxic substances, since no chromates are employed.
  • the rinse water may be treated with standard metal recovery methods such as ion exchange, reverse osmosis, or electrodialysis, and hence recycled 9.
  • FIG. 1 A comparison with Figure 1 shows that for the typical example shown, the present invention eliminates five water rinse stages, a neutralising rinse, an acid rinse 4, and the chromate treatment.
  • the present invention thus greatly reduces the consumption of water and electricity, since far less solution requires heating, and also uses much less space for plating vessels, tanks, and other equipment.
  • toxic chromates are eliminated, thus greatly simplifying waste treatment.
  • Figure 3 shows a process in accordance with the present invention, expressed as a current-time chart.
  • a current 10 is applied to an article 2 and the metal ions that form the coating are reduced on the cathode to the metallic form to provide the coating layer 7.
  • the value of the currents required for electrodeposition purposes '" will be known to those skilled in the art, and depend partly on the metal or metals of interest. Typical current densities range between 0. lA/dm 2 and 10A/dm 2 , however, values outside of this range may also be suitable. For some metal ions it may be desirable or necessary to vary the current during the electrodeposition stage.
  • one option is to turn off the current 11 at this point the article 2 is plated with the coating 7.
  • the coated article remains in contact with the solution for a period 12 and it is during this period 12' that the passivation film 8 is formed.
  • FIG. 4 shows another example of a process . in accordance with the present invention wherein a current flow is not reduced to zero during passivation.
  • a sufficient current is passed through the plating cell " "to permit the reduction of metal ions to form the desired coating 10.
  • the cathode voltage 13 will be at or below the reduction potential 14 required for the deposition of the metal ions.
  • the current is reduced 11 such that the cathode voltage shifts to a value that is nobler than the reduction potential of the metal ions involved 15. If necessary, the cathode potential can be measured using a commercially available reference electrode.
  • Figure 5 shows an example of a process in accordance with the present invention for the formation of multi- layered coatings comprising of alternate layers of electrodeposited coating and passivation film.
  • These coating systems possess a range of properties, including exceptionally high corrosion resistance, partly since the coatings contain in-built passivation films that act to suppress corrosive. attack.
  • - IB - The first cycle shows the application of current .10 to permit electrodeposition. This forms the coating 7 on the substrate 2. The current is then turned off 11 and the passivation period 12 commences. During this time, the passivation film 8 is formed on the electrodeposited layer.
  • the second cycle begins immediately at the end of the first cycle, and current re-applied. This produces an electrodeposited layer 16 on the passivation film 8.
  • the passivation stage of ' the second cycle generates a passivation film 17 on the underlying electrodeposited coating.
  • the passivation film formed during cycle 1 thus becomes an interlayer between two electrodeposited coating layers.
  • the third cycle is then carried out, and this produces an article furnished with six layers of alternating electrodeposited coating and passivation film 18.
  • the three cycles are shown only for illustrative purposes and any number of successive cycles can be performed.
  • the length of time over which either the electrodeposited coating or passivation filmed are formed can be varied such that the cycles times can be adjusted for a particular application.
  • the technique illustrated by Figure 4 may also be employed if desired.
  • Figure 6 shows a plating cell 21 • containing a solution 22.
  • circulation pumps 23 are positioned within the cell 21.
  • the pumps 23 are configured such that the movement of the solution 22 that subsequently arises from their operation is such that the solution. is directed towards the walls of the plating cell, shown by arrows 24.
  • the resulting turbulence produces gentle agitation around the sample to be plated 25.
  • a distance of 3m between the pumps and lm from the mid point between the pumps is shown. Suitable alternative configurations and agitation methods may be employed as appropriate.
  • Example 1 Example 1
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , lOOg/L ammonium chloride, NHC1, lg/L sodium molybdate, Na 2 Mo0 , lg/L ammonium peroxodisulphate (NH 4 ) 2 S 2 0 8 , and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes, which was sufficient to provide a zinc deposit of approximately 10 ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 2 minutes, during which time the passivation film was observed to form on the coating surface.
  • the resulting passivation film was blue in colour, with a bright reflective appearance.
  • Example 3 The solution and process described in Example 1 was repeated, however, on this occasion the time period over which passivation was carried out was 8 minutes, as opposed to 2 minutes. The 8-minute passivation period resulted in the formation of a bright yellow passivation film.
  • Example 3 The solution and process described in Example 1 was repeated, however, on this occasion the time period over which passivation was carried out was 8 minutes, as opposed to 2 minutes. The 8-minute passivation period resulted in the formation of a bright yellow passivation film.
  • Example 2 The solution and process described in Example 1 was repeated, however, on this occasion the time period over which passivation was carried out was 12 minutes, • as opposed to 2 minutes.
  • the 12-minute passivation period resulted in the formation of a bright purple passivation film.
  • Example 1 The solution and process described in Example 1 was repeated, however, on this occasion the time period over which- passivation was carried out was 18 minutes, as opposed to 2 minutes.
  • the 18-minute passivation period resulted in the formation of a bright green passivation film.
  • Example 5 The solution and process described in Example 1 was employed. Again the solution was maintained at 20°C and commercial grade zinc anodes were used. Prior to plating, a standard commercially available saturated calomel reference electrode was immersed into the solution, and connected to the negative terminal of a voltmeter.
  • a mild steel, article was immersed in the solution and electroplating carried out ⁇ at lA/dm2 for 20 minutes.
  • the positive terminal of the voltmeter was connected to the steel cathode, and a reading of -1.30V was obtained during electroplating.
  • the current was turned off after 20 minutes, and the open .circuit voltage of the fresh zinc coating was -1.01V.
  • current was again applied such that the voltage was held at A.11V. This represented the application of a cathodic overvoltage to the zinc coating of 0.1V.
  • the cathodic overvoltage was applied for 5 minutes, during which time, the passivation film was observed to form. A bright pink coloured passivation film was obtained.
  • Example 1 The solution in Example 1 was employed, at 20°C and using commercial grade zinc anodes. A steel article was immersed in the solution and electroplating carried out at 2A/dm2 for 2 minutes, sufficient to form a zinc coating of 2(Jm thickness. The current was then turned off. The coated article was then in contact with the solution for a- further 90 seconds, during which time a light yellow passivation film was formed. Instead of removing the passivated and coated article from the solution, electroplating was again carried out at 2A/dm 2 for 2 minutes. The current was then turned off, and an electrodeposited coating had formed over the surface of the underlying light yellow passivation film. The coated article was then in contact with the solution for 90 seconds, during which time a light yellow passivation film was again formed.
  • the resulting multi-layer coating consisted of five 2 ⁇ m thick zinc layers, with four passivation films alternating between the zinc layers, and an outer bright violet passivation film.
  • a water solution comprised lOOg/L zinc chloride, lg/L sodium tungstate, lg/L sodium metavanadate, lg/L sodium periodate, 5g/l thiamine hydrochloride, and 5g/L sodium thiosulphate.
  • the solution was maintained at 25°C.
  • Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes, which was sufficient to provide a zinc deposit of approximately 10 ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 2 minutes, during which time a passivation film was observed to form on the coating surface.
  • the resulting passivation film was pale blue in colour, with a bright reflective appearance.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 45g/L nickel chloride, NiCl 2 , lOOg/L ammonium chloride, NHC1, lg/L sodium olybdate, Na 2 Mo0 4 , lg/L ammonium peroxodisulphate (NH ) 2 S 2 0 8 , and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes, which was sufficient to provide a zinc-10 weight percent nickel alloy deposit of approximately 10 ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 5 minutes, during which time a passivation film was observed to form on the coating surface.
  • the resulting passivation film was an intense purple colour, with a bright reflective appearance.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 20g/L cobalt chloride, CoCl 2 , lOOg/L ammonium chloride, NH 4 C1, lg/L sodium molybdate, Na 2 Mo0 , lg/L ammonium peroxodisulphate (NH ) 2 S 2 0 8 , and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes t which was sufficient to provide a zinc-0.6 weight percent cobalt alloy deposit of approximately 10 ⁇ m thickness. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 6 minutes, during which time a passivation film was observed to form on the coating surface . _ ⁇ 4 -
  • the resulting passivation film was an intense yellow-orange colour, with a bright reflective appearance.
  • a water solution comprised 8g/L zinc oxide, 90g/L sodium hydroxide, NaOH, lg/L sodium molybdate, Na 2 Mo0 4 , lg/L sodium tungstate, NaW0 , lg/L ammonium peroxodisulphate (NH ) 2 S 2 0 8 , and lmL/L 30 Vol hydrogen peroxide.
  • the solution was maintained at 25°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 10 minutes, which was sufficient to provide a zinc deposit of approximately 8 ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 15 minutes, during which time a bright blue passivation film was observed to form on the coating surface.
  • Example 11 A water solution comprised 188g/L copper sulphate, CuS0. 5H 2 0, 75g/L sulphuric acid, lg/L sodium molybdate, NaMo0 4 , lg/L sodium vanadate, NaV0 3 , and 2.5g/L sodium metabisulphite, Na 2 S 2 0 6 2, and lg/L ammonium peroxodisulphate, (NH 4 ) 2 S 2 0 8 .
  • the solution was maintained at 40°C.
  • Commercial grade bagged copper anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at 5A/dm 2 for 2 minutes, which was sufficient - - to . provide a copper deposit of approximately 10 ⁇ m.
  • the current was turned off, and the coated article permitted to remain immersed in the solution for a further 15 minutes, during which time a bright red passivation film was observed to form on the coating surface.
  • a water solution comprised 72g/L stannous sulphate, 50g/L sulphuric acid, 40g/L phenolsulphonic acid, 2g/L gelatin, lg/L beta-napthol, lg/L sodium molybdate, Na 2 Mo0 4 , and lg/L ammonium peroxodisulphate, (NH ) S 2 0 8 .
  • the solution was maintained at 23°C.
  • Commercial grade tin anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 10 minutes, which was sufficient to provide a tin deposit of approximately 5 ⁇ m.
  • the current was turned off, and the coated article permitted to remain immersed in the' solution for a further 8 minutes, during which time a bright yellow passivation film was observed to form on the coating surface.
  • a water solution comprised lOOg/L-manganese sulphate, 75g/L, 60g/l ammonium thiocyanate, lg/L sodium molybdate, Na 2 Mo0 4 , and lg/L ammonium peroxodisulphate, (NH ) 2 S 2 0 8 .
  • the solution was maintained at 25°C.
  • Commercial grade stainless steel " anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at 2A/dm 2 for 20 minutes, which was sufficient to provide a manganese deposit of approximately 10 ⁇ m.
  • the current was turned off, and the coated article permitted to remain immersed in the solution for a further 8 minutes, during which time a bright red-green passivation film was observed to form on the coating surface.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , lOOg/L ammonium chloride, NH 4 C1, lg/L sodium molybdate, Na 2 Mo0 4 , lg/L ammonium peroxodisulphate (NH 4 ) 2 S 2 0 8 , and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes, which was sufficient to provide a zinc deposit of approximately 10 ⁇ m. The current was turned off, and the coated article removed from the solution.
  • the un-passivated zinc coating was bright and reflective, with a slight blue tint when angled in light.
  • a water solution comprised 60g/L zinc chloride, 150g/L ammonium chloride, l.Og/L sodium molybdate, and l.Og/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes. The current was then turned off, and the coated article permitted to remain immersed in the static solution for a further 3 minutes, after which it was removed, rinsed, and dried.
  • a water solution comprised 60g/L zinc chloride, 150g/L ammonium chloride, l.Og/L sodium tungstate, and l.Og/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes. The current was then turned off, and the coated, article permitted to remain immersed in the static solution for a further 8 minutes, after which it was removed, rinsed, and dried.
  • the result was a zinc coating furnished with a light golden colour passivation film.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 150g/L ammonium chloride, NHC1, l.Og/L sodium molybdate, l.Og/L ammonium peroxodisulphate, lg/L sodium lauryl sulphate, ' and lg/L sodium metabisulphite.
  • the solution was maintained at 20°C.
  • Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution- and electroplating carried out. The current density initially applied was 0.5A/dm 2 for 5 minutes under static conditions. The current ⁇ density was then immediately increased to l.OA/dm 2 . After 5 minutes of plating at this current density under static conditions, circulation pumps were activated.
  • the resulting coating comprised a 12-micron thick zinc coating furnished with a bright yellow passivation film.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 150g/L ammonium chloride, NHC1, l.Og/L sodium molybdate, l.Og/L ammonium peroxodisulphate, lg/L sodium lauryl sulphate, and lg/L sodium metabisulphite.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out. The current density initially applied was 0.5A/dm 2 for 5 minutes under static conditions. The current density was then immediately increased to l!0A/dm 2 . After 5 minutes of plating at this current density under static conditions, circulation pumps were activated' such that gentle turbulence was produced around the article, and which was not unidirectional. After a period, of lOminutes of further plating at l.OA/dm 2 , the pumps were turned off and static conditions restored. A final plating period of 2 minutes at l.OA/dm 2 followed. The current was then turned off, and the coated article permitted to remain immersed in the solution. The circulation pumps were then reactivated for a period of 3 minutes, during which time a passivation film was observed to form on the coating surface.
  • the resulting coating comprised a 12-micron thick zinc coating furnished with a bright yellow-purple passivation film with an attractive mottled appearance.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 150g/L .ammonium chloride, NH 4 C1, l.Og/L sodium molybdate, l.Og/L ammonium ' peroxodisulphate, lg/L sodium lauryl sulphate, and lg/L sodium metabisulphite.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at 1.0 A/dm 2 for a period of 10 minutes.
  • the bus bar holding the steel article was moved by approximately 5 cm from its original position, in • a sideways movement. This action assisted in the removal of any hydrogen bubbles from the surface and any streaking effects • they may otherwise have caused.
  • the current was then turned off,' and the coated article permitted to remain immersed in the static solution for a further 8 minutes, during which time a passivation film was observed to form on the coating surface.
  • the resulting coating comprised a 12 micron thick zinc coating furnish with a bright yellow passivation film, where the colour was uniform over the entire sample surface.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , 150g/L ammonium chloride, NH 4 C1, 0.8g/L sodium molybdate, 0.8g/L ascorbic acid, and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 20 minutes. To promote the formation of the electrodeposited zinc coating, during the initial 10 minutes of electroplating, the solution was maintained in a static condition. Circulation pumps were then activated as described in Example 16, and plating continued under conditions of solution agitation. After 8 minutes under these conditions, the pumps were turned off, and plating continued for a further 2 minutes under static conditions. The current was then turned off, and the coated article permitted to remain immersed in the static solution for a further 8 minutes, during which time a passivation film was observed to form on the coating surface. The resulting coating comprised a 10 micron thick zinc coating furnish with a bright purple-green passivation film.
  • Example 21 Example 21
  • a water solution comprised 60g/L zinc chloride,
  • ZnCl 2 150g/L ammonium chloride, NH 4 C1, l.Og/L sodium molybdate, l.Og/L salicylic acid, and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 20 minutes. To promote the formation of the electrodeposited zinc coating, during the initial 10 minutes of electroplating, the solution was maintained in a static condition. Circulation pumps were then activated as described in Example 16, and plating continued under conditions of solution agitation. After 8 minutes under these conditions, the pumps were turned off, and plating continued for a further • 2 minutes under static conditions. The current was then turned off, and the coated article permitted to remain immersed in the static solution for a further 8 minutes, during which time a passivation film was observed to form on the coating surface.
  • the resulting coating comprised a 10 micron thick zinc coating furnish with a bright purple-green passivation film.
  • Example ⁇ i A water solution comprised 60g/L zinc chloride, 15g/L nickel chloride, lOOg/L potassium chloride, 0.8g/L sodium molybdate, 0.8g/L ascorbic acid, and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 40°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 20 minutes. To promote the formation of the electrodeposited zinc-rich alloy coating, during the initial 10 minutes of electroplating, the solution was maintained in a static condition. During the following 8 minutes of electroplating, the solution was agitated through the use of circulation pumps . The final two- minute period of plating was carried out with the pumps turned off. The current was then turned off, and the coated article permitted to remain immersed in " the solution for a further 8 minutes, during which time the passivation film was observed to form on the coating surface.
  • the resulting coating comprised a 10-micron thick zinc-10 weight per cent nickel alloy coating furnish with a bright yellow-purple passivation film.
  • Example 20 The solution in Example 20 was employed, at 20°C and using stainless steel anodes. A steel article was immersed in the static solution and electroplating carried out under static conditions at lA/dm 2 for 60 seconds, sufficient to form a 0.5 ⁇ m zinc coating. The current was then turned off. The coated article was then in contact with the solution for a further 60 seconds, during which time a light blue passivation film was formed. Instead of removing the passivated and coated article from the solution, electroplating was again carried out at lA/dm 2 for 60 seconds. The current was then turned off, and an electrodeposited coating, had formed over the surface of the underlying passivation film.
  • Electroplating at lA/dm 2 for 60 seconds, followed by passivation for 60 seconds was repeated seven times. Electroplating at lA/dm 2 for 5 minutes was then carried out with circulation pumps activated. The current and the pumps were then turned off. A final passivation film was produced through contact with the solution for 8 minutes under static conditions, which yielded a bright yellow passivation film.
  • the resulting coating comprised multiple 0.5 ⁇ m thick zinc layers, with passivation films sandwiched between the zinc layers, and an outer bright yellow passivation film.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , lOOg/L ammonium chloride, NH4CI, 0.2g/L sodium molybdate, 0.8g/L sodium tungstate, lg/L sodium lauryl sulphate surfactant, lg/L sodium metabisulphite, and O.lg/L thiamine hydrochloride .
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution and electroplating carried, out at lA/dm2 for 20 -minutes, during which time circulation pumps were operated continuously. The current was turned off, and the coated article permitted to remain immersed in the agitated solution for a further 2 minutes, during which time a passivation film was observed to form on the coating surface. The result was a zinc deposit of approximately 10 ⁇ m furnished with a lilac coloured passivation film.
  • Example 25 A water solution comprised 60g/L zinc chloride, ZnCl 2 , lOOg/L ammonium chloride, NH 4 C1, 0.2g/L sodium molybdate, 0.8g/L sodium tungstate, lg/L sodium lauryl sulphate surfactant, lg/L sodium metabisulphite, and O.lg/L thiamine hydrochloride.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 20 minutes, during which time circulation pumps were operated continuously. The current was turned off, and the coated article permitted to remain immersed in the agitated solution for a further 6 minutes, during which time a passivation film was observed to form on the coating surface.
  • a water solution comprised 60g/L zinc chloride, 15g/L cobalt chloride, 150g/L 'ammonium chloride, 0.2g/L - 3b - sodium molybdate, 0.8g/L sodium tungstate, and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 30°C. Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 20 minutes, during which time circulation pumps were operated continuously. The current was turned off, and the coated article permitted to remain immersed in the agitated solution for a further 2 minutes, during which time a passivation film was observed to form on the coating surface.
  • Example 27 A water solution comprised 60g/L zinc chloride, ZnCl 2 , 150g/L ammonium chloride, NHC1, 0.2g/L sodium molybdate, 0.8g/L sodium tungstate, lg/L sodium lauryl sulphate surfactant, lg/L sodium metabisulphite, and O.lg/L thiamine hydrochloride.
  • the solution was employed at 20°C and using commercial zinc anodes.
  • a steel article was immersed in the solution, with circulation pumps activated, and electroplating carried out under static conditions at lA/dm 2 for 60 seconds, sufficient to form a 0.5 ⁇ m zinc coating.
  • the current was then turned off.
  • the coated article was then in contact with the solution for a further 60 seconds, during which time a dark yellow passivation film was formed.
  • electroplating was again carried out at lA/dm 2 for 60 seconds. The current was then turned off, and an electrodeposited coating had formed over the surface of the underlying passivation film.
  • a water solution comprised 60g/L zinc chloride, llOg/L potassium chloride, 0.2g/L sodium molybdate, 0.8g/L sodium tungstate, 0.2g/L ascorbic acid, 0.15g/L ammonium peroxodisulphate, and lg/L sodium lauryl sulphate surfactant.
  • the solution was maintained at 20°C. Commercial grade zinc anodes were used.
  • a mild steel article was immersed in the solution and electroplating carried out at lA/dm 2 for 20 minutes, during which time circulation pumps were operated continuously. The current was turned off, and the coated article permitted to remain immersed in the agitated solution for a further 2 minutes, during which time a passivation film was observed to form on the coating surface.
  • the result was a zinc deposit of approximately lO ⁇ m thickness furnished with a bright iridescent passivation film.
  • Example 29 A water solution comprised 188g/L copper sulphate (CuS0. 5H 2 0), 75g/L sulphuric acid, 0.4g/L sodium molybdate, 1.2g/l sodium tungstate, 2.5g/L sodium metabisulphite, and 0.2g/L sodium lauryl sulphate. The solution was maintained at 40°C. Commercial grade bagged copper anodes were used. A mild steel article was immersed in the static solution and electroplating carried out at 5A/dm2 for 2 minutes, which was sufficient to provide a copper deposit of approximately lO ⁇ m thickness. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 5.5 minutes, during which time a yellow passivation film was observed to form on the coating surface.
  • CuS0. 5H 2 0 copper sulphate
  • 0.4g/L sodium molybdate 1.2g/l sodium tungstate
  • 2.5g/L sodium metabisulphite 2.5g/L sodium metabisulph
  • a water solution comprised 72g/Lstannous sulphate, 50g/L sulphuric acid, 40g/L phenolsulphonic acid, 2g/L gelatin, lg/L beta-napthol, 0.5g/L sodium molybdate, and 0.6g/L sodium tungstate.
  • Example 31 The solution was maintained at 25°C. Commercial grade tin anodes were used. A mild steel article was immersed in the solution and electroplating carried out at lA/dm2 for 10 minutes under static conditions. This was sufficient to provide a tin deposit of approximately 6 ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 4 minutes, during which time a bright yellow passivation film was observed to form on the coating surface .
  • Example 31 Example 31
  • a water solution comprised lOOg/L manganese sulphate, 75g/L ammonium thiocyanate, 0.4g/L sodium molybdate, and 1.2g/L sodium tungstate.
  • the solution was maintained at 25°C. Commercial grade stainless steel anodes were used. A mild steel article was immersed in the solution and electroplating carried out at 2A/dm 2 for 20 minutes, which was sufficient to provide a manganese deposit of approximately lO ⁇ m. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 5 minutes, during which time a bright red-green passivation __ film was observed to form on the coating surface.
  • a water solution comprised 300g/L nickel sulphate, 40g/L nickel chloride, 35g/L boric acid ? O.lg/L sodium lauryl sulphate, 0.2g/L sodium molybdate, and 0.8g/L sodium tungstate.
  • the solution was maintained at 55°C. Commercial grade nickel anodes were used. A mild steel article was immersed in the static solution and electroplating carried out at 5A/dm 2 for 10 minutes. The current was turned off, and the coated article permitted to remain immersed in the solution for a further 4 minutes, again under static conditions, during which time an iridescent yellow passivation film was observed to form on the coating surface.
  • a water solution comprised 60g/L zinc chloride, ZnCl 2 , lOOg/L ammonium chloride, NHC1, 0.2g/L sodium molybdate, 0.8g/L sodium tungstate, lg/L sodium lauryl sulphate surfactant, lg/L sodium metabisulphite, and ' O.lg/L thiamine hydrochloride.
  • the solution was maintained at 25°C. Commercial grade zinc anodes were used. A mild steel article was immersed in the solution with circulation pumps activated. A current density of 2 A/dm 2 was applied for 15 minutes. The current was then turned off and the sample removed, followed by rinsing and drying.
  • the result was a zinc coating of approximately 10 microns thickness.
  • the first test conducted was to allow comparison of corrosion resistance.
  • the samples were placed- in separate baths of aerated 5 percent sodium chloride solution.
  • the time to failure was determined as the time to the formation of red rust corrosion products, namely the point where the coating had failed and permitted the corrosion of the underlying steel.
  • the second test was conducted on a separate batch of samples, and involved applying adhesive tape to the surface. If on pulling back the tape, none of the underlying coating or film was visible on the tape, then this indicated adequate adhesion. Any signs of the coating or film on the tape indicated adhesion failure.
  • the third test again required a separate batch.
  • .epoxy paint was applied to the coating or film surface.
  • the paint was crosshatched several times with a sharp knife.
  • the adhesion tape tests were then applied as above. If on pulling back the tape, none of the paint was visible on the tape, then this indicated adequate adhesion of the paint to the underlying coating or film. Any signs of the paint on the tape indicated adhesion failure.
  • the table shows that commercial un-passivated zinc coatings developed red rust, i.e. the corrosion products of the underlying steel substrate, in 48 ' hours. In contrast, un-passivated zinc coatings from the solution of Example 14 prevented red rust for 144 hours i.e. a three-fold improvement over commercial zinc.
  • These findings confirm that zinc coatings produced from solutions of the present invention are more corrosion resistant than those produced from conventional electroplating solutions. It is considered that a small concentration of the film forming species are integrated within the zinc coating during electrodeposition. These film forming species are further considered to leach from the zinc coating during contact with a corrodent, and act to inhibit corrosion, thereby accounting for the improved levels of corrosion resistance.
  • Example 6 refers to a multi-layer coating. This coating comprises five 2 ⁇ m thick zinc layers, with four passivation films alternating between the zinc layers, and an outer bright violet passivation film.
  • This multilayer coating exhibited corrosion resistance approaching three times that of chromated zinc of the same overall thickness.
  • the penetration of the outer passivation film and the outer zinc layer does not lead to coating breakdown, as is the case with conventional coatings consisting of a single zinc layer with a single passivation film. Instead, the corrodent comes into contact with a further protective passivation film. Indeed the corrodent must penetrate through ten separate layers of either zinc or passivation film before the steel is exposed, as opposed to just two layers with a conventional coating system. The ten separate layers thus act as a brake on the progress of corrosion through the coating, thus accounting for the superior corrosion resistance observed.
  • Example 14 the un-passivated zinc coating produced . according to the present invention, demonstrated excellent paint adhesion. This is considered to arise from the greatly reduced tendency of zinc coatings of the current invention to oxidise in the atmosphere. Paint adhesion to chromate and the passivated coatings of the current invention .(Examples 1, 2, 3 and 6) was found to be excellent with no signs of adhesion loss.
  • Example 15 The coatings and films that were produced from solutions containing molybdate alone (Example 15) afforded an . improvement in corrosion resistance over commercial zinc.
  • the film adhesion to the underlying coating, and ' paint adhesion were both found to be acceptable.
  • the corrosion resistance found with tungstate (Example 16) was of a similar order to that found with molybdate (Example 15), however, the main difference was that paint adhesion to the 'tungstate films' was found to be comparatively less.
  • Example 20 was produced in the presence of solutions containing molybdate and ascorbic acid.
  • the corrosion resistance of the coatings and films was slightly lower than found with those films of similar colour produced in the presence of molybdate and peroxide salt (e.g. Example 3), however, film adhesion and paint adhesion were satisfactory.
  • Example 33 was produced from solutions containing molybdate and tungstate, however, no film was permitted to form.
  • the resistance to red rust formation seen with this example exceeded that of Example 14, namely a zinc coating of similar thickness produced from a solution containing molybdate and peroxide salt. This suggests that the combination of molybdate and tungstate has a particularly beneficial effect on corrosion resistance.
  • Example 24 the coatings were produced with passivation films from solutions containing molybdate and tungstate. In all of the- tests, these samples performed in a similar manner to those produced from molybdate - peroxo salt containing solutions.
  • Example 27 related to a multi-layer comprising thin layers of zinc with a passivation film between each layer, and an outer bright yellow passivation film. The most interesting test result for this sample was in terms of corrosion resistance. The corrosion test was halted after 2000 hours, since no red rust had been observed after this substantial time period, which was around three times longer than that seen for the chromated zinc control sample. It is thought that the presence of the corrosion resistant passivation films within the zinc coating is largely responsible for the major improvements seen in the corrosion test, particularly when compared

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Abstract

L'invention concerne une solution électrolytique comprenant au moins un ion de métal à dépôt électrolytique pouvant être réduit à la forme métallique, au moins une espèce d'ion de métal de transition, et un solvant. Un revêtement passivé dudit ion de métal à dépôt électrolytique peut être déposé sur un article.
PCT/GB2003/003160 2003-07-23 2003-07-23 Solution electrolytique Ceased WO2005014890A1 (fr)

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Cited By (7)

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Publication number Priority date Publication date Assignee Title
WO2011036260A2 (fr) 2009-09-24 2011-03-31 Stefan Dameron Procédé de galvanisation et de passivation
US8936770B2 (en) 2010-01-22 2015-01-20 Molycorp Minerals, Llc Hydrometallurgical process and method for recovering metals
WO2017086767A1 (fr) * 2015-11-20 2017-05-26 Ontiveros Balcázar Alberto Manuel Procédé pour appliquer une pluralité de couches de revêtement sur des bandes métalliques au moyen d'un système d'électroplacage
CN108754555A (zh) * 2018-08-29 2018-11-06 广东天承科技有限公司 一种电镀液及其电镀方法
CN109972186A (zh) * 2019-03-04 2019-07-05 东莞市凯盟表面处理技术开发有限公司 一种不锈钢钝化处理方法
CN111575047A (zh) * 2020-05-08 2020-08-25 浙江大学 一种异构化油的分离方法
CN114292128A (zh) * 2021-12-22 2022-04-08 同济大学 一种用于电化学修复混凝土裂缝的溶液及其制备方法

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GB1319912A (en) * 1970-12-15 1973-06-13 Toyo Kohan Co Ltd Electroplated steel sheet
SU1696581A1 (ru) * 1989-04-24 1991-12-07 Предприятие П/Я М-5876 Электролит дл гальванического осаждени медного покрыти
JPH07292491A (ja) * 1994-04-21 1995-11-07 Hitachi Cable Ltd 高耐食性めっき皮膜およびめっき液

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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011036260A2 (fr) 2009-09-24 2011-03-31 Stefan Dameron Procédé de galvanisation et de passivation
DE102009044982A1 (de) 2009-09-24 2011-03-31 Stefan Dameron Verfahren zum Galvanisieren und zur Passivierung
WO2011036260A3 (fr) * 2009-09-24 2011-06-16 Stefan Dameron Procédé de galvanisation et de passivation
US10179942B2 (en) 2010-01-22 2019-01-15 Secure Natural Resources Llc Hydrometallurgical process and method for recovering metals
US8936770B2 (en) 2010-01-22 2015-01-20 Molycorp Minerals, Llc Hydrometallurgical process and method for recovering metals
WO2017086767A1 (fr) * 2015-11-20 2017-05-26 Ontiveros Balcázar Alberto Manuel Procédé pour appliquer une pluralité de couches de revêtement sur des bandes métalliques au moyen d'un système d'électroplacage
CN108754555A (zh) * 2018-08-29 2018-11-06 广东天承科技有限公司 一种电镀液及其电镀方法
WO2020042613A1 (fr) * 2018-08-29 2020-03-05 广东天承科技有限公司 Solution d'électroplacage et procédé d'électroplacage l'utilisant
CN108754555B (zh) * 2018-08-29 2020-04-28 广东天承科技有限公司 一种电镀液及其电镀方法
CN109972186A (zh) * 2019-03-04 2019-07-05 东莞市凯盟表面处理技术开发有限公司 一种不锈钢钝化处理方法
CN109972186B (zh) * 2019-03-04 2020-07-28 东莞市凯盟表面处理技术开发有限公司 一种不锈钢钝化处理方法
CN111575047A (zh) * 2020-05-08 2020-08-25 浙江大学 一种异构化油的分离方法
CN111575047B (zh) * 2020-05-08 2021-03-23 浙江大学 一种异构化油的分离方法
CN114292128A (zh) * 2021-12-22 2022-04-08 同济大学 一种用于电化学修复混凝土裂缝的溶液及其制备方法

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