ZN-BASED COMPOSITE-PLATED METALLIC MATERIAL AND PLATING METHOD

Abstract: A Zn-based composite plating is carried out simultaneously with deposition of Zn and of metallic compounds by a cathode precipitation reaction. This plating is advantageous over conventional Zn or Zn alloy plating having a disadvantage of low sacrificing anode protection at a high content of noble metal and over a conventional dispersion plating having a disadvantage of low co-depositiion degree. The inventive plating attains improved, corrosion-resistance, paintability, formability and adaptability to post-treating.

Description: 1.Field of Invention The present invention relates to a Zn-based composite-plated metallic material exhibiting improved, corrosion-resistance and other properties and to a composite plating method. The present invention relates to mainly steel materials plated with Zn or Zn alloy. Specifically, the present invention relates to a Zn-electroplated steel sheet exhibiting improved, corrosion-resistance, paint-adherence, formability, and other properties, as well as a method for producing said steel sheet. 2. Description of Related Arts The Zn-electroplating is mainly carried out as the rust-proofing plating of steel sheets and has been broadly used in the field of automobiles, household appliances, and the like, by utilizing the sacrificing (galvanizing) anode effect of the Zn coating on the Zn-plated steel sheet. Advantageously, the Zn electroplating is superior to the other plating methods, such as hot-dip galvanizing, in uniformity, formability, smoothness, and the like of coating and enables thin deposition. Nevertheless, along with demands for further improving the corrosion-resistance and the other properties centered recently on automobile bodies have been enhanced, it became more important to develop Zn-based electrolytic plating having further higher properties than the pure Zn plating. Such a method is known from Japanes unexamined patent application No. 60-128 283 which relates to the production of a corrosion resistant Zn or Zn-alloy series electroplated steel sheet, wherein a trivalent Ti compound and a tetravalent Ti are added to the electroplating bath for plating Zn or Zn-alloy in specific amounts. The technical developments, which have been made in the field of plating so as to meet the above demands and to improve such surface properties as the corrosion-resistance and paint-adherence of Zn-electroplated steel sheets are roughly classified into two methods. One of them is already broadly employed for a composite electroplating, and resides in alloy-plating by means of a plating bath, in which such metallic ions as Sn, Pb, Ni, Mo, Mn, Fe, Cu, Co, Cd, and the like capable of codepositing with Zn are incorporated. The other is a dispersion-plating method with the use of additives of organic resin or inorganic material. As the inorganic materials used, fine particles of compounds insoluble to the bath, such as alumina, silica, and the like are suspended and dispersed in the bath. Since, in the ordinary Zn-plated steel sheets, the potential difference between the constituent Zn of plating layer and the Fe as the substrate material is great, the sacrificing anode-effect of the plating layer is excellent. This fact, however, makes it necessary to form an extremely thick plating layer for the purpose of rust-proofing over a long period of time, because the dissolution rate of Zn-plating layer is rapid. The Zn-alloy plating method of Ni, Co, Fe, and the like is presently used to cope with the above described problems, and is based on the concept that the potential difference between the substrate material and plating layer is appropriately controlled by means of depositing, together with Zn, a metal which is electrochemically more noble than Zn, thereby adjusting the sacrificing anode-current (galvanic current) within an appropriate range and hence controlling the corrosion rate of plating layer as low as possible. The presently used, Zn-alloy plating method intends therefore to attain mainly the electrochemical, sacrificing corrosion-proofing. Therefore, the Zn-based alloy plating allegedly exhibits a corrosion-resistance over a longer period of time compared with the ordinary Zn-plated steel sheet, under the identical deposition amounts. Nevertheless, the Zn-based alloy plating involves a limitation in improvement of the corrosion resistance, since a too high content of noble metal incurs a decrease in the sacrificing anode effect, resulting in the pitting corrosion is liable to occur. In addition, a uniform dissolution of the respective elements of the plating layer is a premise for realizing the excellent corrosion resistance of the Zn-based alloy. Actually, however, a preferential dissolution of Zn, which is potentially less noble, occurs, with the result that the proportion of noble metal(s) to less noble metal(s) of the plating layer increases, and finally the potential of the plating layer arrives that of noble metal(s). In this case, the galvanic corrosion-proofing of the iron of substrate is lost. This is presumably a reason for the pitting corrosion described above. In the dispersion plating method, the fine particles of silica, titanium oxide, and the like are dispersed in the liquid body and are incorporated in the plating layer, thereby lessening the electric conductivity and hence suppressing the corrosion speed of a plating layer to the level as low as possible. This technique involves a difficulty in effectively incorporating the fine particles in the plating layer. In addition, since the fine particles used must be chemically inactive so as to prevent dissolution thereof in the plating liquid, the effects of composite particles are principally attributable to physical protection, alone. This provides a limitation in improvement of the corrosion resistance. Incidentially, Al is not capable of co-depositing with Zn (c.f. Iron and Steel Handbook, 3rd Edition, Volume VI, page 419, Fig. 10,27). However, according to a known technique for providing a Zn-Al composite, electroplated steeel sheet, the form of Al in the plating bath is modified to a special one so as to co-deposit the same together with Zn. The metallic Al particles, which are dispersed in a plating layer, have a property of being liable to dissolve during the corrosion. This property is utilized to chemically and electrochemically enhance the rust-proofing. More specifically, in Japanese Examined Patent Publication No. 54-30649, there is disclosed a technique for forming a Zn-Al composite electroplating containing 1.5 to 70% by weight of the dispersed Al, by means of stirring the Zn plating bath, in which the Al powder is suspended. The technique described in this publication has common characteristics of alloy plating and dispersion plating. The structure of obtained plating is however so prominent that Al is enriched and segregated in the top surface side of a Zn-Al composite electroplated layer, and such Al allegedly improves the corrosion-resistance according to the description of publication. In addition, according to Japanese Unexamined Patent Publication No. 60-125,395, there is a technique disclosed for forming a Zn-alumina series composite plating containing, in terms of Al₂O₃, from 0.01 to 3% by weight of aluminum compound, which is soluble to dilute hydrochloric acid, by use of the plating bath, in which positively charged alumina sol is added. As is described above, the alloy plating involves a tendency that the galvanic corrosion-protection by Zn is weakened by the alloyed noble metal. The mere alloying of a plating layer therefore involves a limitation in the improvement of corrosion resistance. In the dispersion plating of fine particles, the fine particles of 5 µm 50 µm in diameter are positively charged by means of a cationic surfactant agent and moves toward the surface of a cathode due to electrophoresis, and deposits on the electrode surface while losing the charges. The fine particles may have positive charges due to the inherent characteristics thereof. The deposits on the electrode surface are merely physically adsorbed due to the Van der Waals force with respect to the electrode surface. Contrary to this, the bonding between the deposited plating metal and the constituent metal of an electrode is metallic bond. Accordingly, the fine particles can easily separate from the electrode surface, until such a deposition state of matrix metal that the fine particles are embedded therein at a half or more of the diameter of fine particles. The drawbacks of the conventional dispersion plating method are therefore as follows. (1) the co-depositing plating is not obtained at a plating thickness of 1/2 or less relative to the diameter of co-deposited particles. (2) Since the separation possibility of co-depositing particles from the physical surface is high during the plating process, a high co-deposition degree is not obtained. In order to obtain a certain co-deposition degree, the content of co-depositing components in the bath must be raised exceedingly. (3) Under the conditions of a high speed-plating (plating at a high current density), strong stirring becomes necessary. This incurs a decrease of the co-deposition degree. (4) With the increase in the particle diameter, the influence of gravity appears, such that, for example in the plating using horizontal electrodes, the co-deposition degree in the lower side is lower than that in the upper side of a workpiece. (5) The solid matter included in the bath makes it difficult to maintain the uniformity of bath components and to maintain the devices. SUMMARY OF INVENTION It is an object of the present invention to develop a novel technique for composite Zn-electroplating; which principally does not have the drawbacks of conventional Zn-plating technique; which is suitable for production of Zn-plated steel sheets in which production a high speed plating is essential; and, which provides a composite plated metallic material exhibiting improved corrosion-resistance and paintability. The present inventors developed a heretofore unknown, composite plating method: in which metallic Zn is applied, by electroplating, on the surface of metallic material to form a film; such metallic compound as hydroxide and phosphates is dispersed and co-deposited in the plating layer at the same time as the Zn-plating; and, the insoluble composite particles are not added to the bath. In the present invention, the presence of solid matter in the plating bath is unnecessary, the composite components of composite plating are present in the bath in the form of ions, such as Al⁺⁺⁺, and, hydroxide and phosphates deposit in accordance with the rise of pH due to discharge of H⁺ at the cathode. This deposition reaction occurs only in an extremely thin diffusion layer on the electrode surface. The hydrogen bonding of water adsorbed on the electrode surface as well as the electric attractive force between the undischarged aluminum ions and the electrode surface are the intermediary for bonding the deposited hydroxide and phosphates, with respect to the electrode surface. This provides a stronger bonding than by merely physical bonding. It is therefore understood that the separation possibility of deposits under physical external force, such as stirring, becomes considerably low. The present invention is therefore principally free of the drawbacks (1) through (5) of the conventional dispersion plating, and is excellent when compared with the conventional dispersion-plating. The superiority of the present invention over the conventional dispersion plating is particularly high in the case of applying the present invention to the production of Zn-plated steel sheets, in which a high speed plating is essential. The Zn-based composite plated metallic material according to the present invention is characterized in that a product of a cathodic precipitation-reaction on said substrate being a compound of at least one ionic metal selected from the group consisting of aluminum, calcium, magnesium, strontium, titanium, zirconium, chromium, tungsten, and molybdenum is contained in said plating layer of zinc or zinc alloy in an amount of from 0.002 to 10% by weight in terms of the metal. Further the invention is directed to a method for plating a Zn-based composite material on a metallic-material substrate, as laid down in independent claim 7. If the content of metallic compound described in detail hereinbelow is less than 0.002% by weight, the composite plating is ineffective. On the other hand, if the content of metallic compound is more than 10% by weight, there is a danger that Zn is not applied by plating. The compound, which is the composite member of a plating layer, is composed by a cathodic precipitation reaction. This is an outstanding feature according to the present invention and is described hereinafter. The pH of the plating bath, which contains aluminum ions, is adjusted to or slightly less than an equilibrium pH of Al(OH)₃-precipitation. The steel sheet as a plating object is electrolyzed in such plating bath, so that the aluminum ions move to the cathode surface due to the potential between the anode and cathode. When the pH on the cathode surface rises, the aluminum ions react with OH⁻, to yield Al(OH)₃ or Al(OH)₃·nH₂O. The particles of Al(OH)₃ or Al(OH)₃·nH₂O are included in the Zn plated film formed. The components of the bath are presumably adsorbed somewhat on the Al(OH)₃·nH₂O particles. In cases where an oxidizer is contained in the bath, the film formation occurs in the same process as the case of aluminum as described above, except that the pH rise at the interface of cathode during electrolysis occurs mainly due to the consumption of H⁺ by its reaction with oxidizer and hence yielding of OH⁻. Accordingly, the simultaneous reactions of film formation occurs in parallel: (1) deposition reaction of metallic Zn, (2) consumption of H⁺ at the interface of cathode, and (3) deposition reaction of composite particles. (1) Deposition Reaction of Metallic Zn Zn 2⁺ + 2e⁻ → Zn (2) Consumption of H⁺ at Interface of Cathode (3) Deposition Reaction of Composite Particles Al³⁺ + 30H⁻ → Al(OH)₃ Ca²⁻ + 20H⁻ → Ca(OH)₂ Mg²⁺ + 20⁻ → Mg(OH)₂ Sr²⁺ + 20H⁻ → Sr(OH)₂ Ti⁴⁺ + 40H⁻ → Ti(OH)₄ Zr⁴⁺ + 40H⁻ → Zr(OH)₄ Cr³⁺ + 30H⁻ → Cr(OH)₃ Mo⁶⁺ + 50H⁻ + e⁻ → Mo(OH)₅ W⁶⁺ + 50H⁻ + e⁻ → W(OH)₅ The reaction (1) is a reduction and deposition of Zn²⁺ and is the principal reaction. This reaction proceeds in the same manner as in the ordinary Zn plating. However, in parallel with this reaction, the oxidizer reacts electrochemically at the cathode interface as in (2), to incur the pH rise at the cathode interface during the electrolysis. Along with this, the reaction (3) proceeds to form a composite film. The composite deposition of aluminum is further promoted by an oxidizer. In the case of using phosphate, the composite deposition of zinc phosphate occurs by the reaction of 3Zn(H₂PO₄)₂ → Zn₃(PO₄)₂↓ + 4H₃PO₄ In addition, such reactions as Al³⁺ + PO₄³⁻→ AlPO₄↓ and Cr³⁺ + PO₄³⁻→ CrPO₄↓ occur. As the oxidizer, the oxyacid such as NO₃⁻, NO₂⁻ and SeO₃⁻, and the halogen acid such as BrO₃⁻, IO₃⁻ and ClO₃⁻ can be used. NO₃⁻ is preferred in the light of stability, i.e., non-decomposition in the bath, and reactivity, i.e., attainment of desired quantity of co-deposition by a small amount. The particular form of these oxyacid and halogen acid to be added into the bath is acid, metallic salt, or ammonium salt. In addition, as the oxidizer, peroxide, such as H₂O₂, hydrogen peroxide-aduct, such as Na₂SiO₃ · H₂O₂ . H₂O or NaBO₂ · H₂O₂·H₂O, and metallic peroxide such as MgO₂ and CaO₂ can be used. The above oxidizing compounds can be used alone or in combination of optionally selected two or more. Furthermore, it is possible to use oxyacid, peroxide, hydrogen peroxide aduct and metallic peroxide other than the above described ones, provided that they realize the desired effects. The characterizing structure of the Al-composite plating film according to the present invention is hereinafter described. The structure of this film is that very fine gel particles of aluminum hydroxide and the like are included in the Zn plated layer as the composite member. When this film is subjected to thorough natural drying, heating or reduced pressure so as to dry the same, the product particles of cathodic precipitation reaction undergo a dehydration, thereby incurring such a gradual change of compound that the " n " of Al(OH)₃·nH₂O decreases or Al(OH)₃ is converted to Al₂O₃. Along with such change, the product particles of cathodic precipitation reaction shrinks, and the hydration-water and the chemically or physically adsorbed water vaporize, with the consequence that a number of minute pores are formed in the alumina gel-particles which are included in the Zn-plating layer. Such structure of composite plated layer according to the present invention is one factor for improving the corrosion resistance. The reasons for the corrosion-resistance improvement are considered as follows. (a) The alumina gel in the film adsorbs the water and then forms a protective coating. (b) When alumina, once calcined at a high temperature, is dispersed in the plating layer, a problem appears in that the alumina slowly dissolves in the acid. Contrary to this, aluminum compound, which deposits by the cathodic precipitation reaction of aluminum ions according to the present invention, is alumina gel which has the properties of extremely easily dissolving in acid and alkali, and, therefore, the Al³⁺ redissolved realizes the effect that it immediately suppresses a conversion reaction of Zn(OH)₂ formed as a result of Zn-corrosion to conductive ZnO. (c) In the conventional, simple Zn plating, Zn²⁺ dissolved by the sacrificing anode effect does not form a protective coating but is liable to move externally and disappear. When the pores are formed in the plating layer by drying in accordance with the present invention, the Zn²⁺ are trapped in the minute pores to form a protective coating. The Zn-Al compound composite plating layer is porous and has a large effective surface area. By utilizing this property, the post-treatment with the use of organic or inorganic sealant can be carried out, to further enhance the properties. The present invention is therefore suitable also for the production of surface-treated steel sheets and paint-coated steel sheets having a high corrosion-resistance. The applications, in which the other functional properties are utilized, are broad, such as black plating for exterior coating and impregnation of lubricant oil, press oil, and the like for producing the heavily worked steel sheets or for surface treatment for cold-working. The method for composite plating according to the present invention is hereinafter described with reference to an example. The Zn-sulfate or chloride bath, and the ordinarily used acidic Zn bath can be used as the Zn-plating bath. The Zn-plating bath contains Zn²⁺ preferably from 2 to 150 g/l. The concentration of metallic ions, such as aluminum, chromium, calcium, and the like is in at least such quantity that the desired improvement of corrosion resistance can be attained. This concentration is at the highest below such quantity that the metallic ions tend to precipitate as the hydroxide and the like, or gel material tends to form to suppress the precipitation of Zn. A preferable concentration within this lowest and highest quantity depends on pH but is, for example, from 0.01 to 50g/l for Al³⁺, Ca²⁺, Cr³⁺, Mg²⁺, and Sr²⁺, and from 0.1 to 20g/l for W⁶⁺, Mo⁶⁺, Ti⁴⁺, and Zr⁴⁺. The forms of metallic ions, such as aluminum ions, suitable for adding into the plating bath are nitrate, chloride, sulfate, and the other soluble metallic salt. Alternatively, the metallic powder may be added to and dissolved in the bath, or the Zn-Al alloy or the like may be used for the anode. When the quantity of oxidizer is too small, its effect is not attained. On the other hand, when the quantity of oxidizer is too large, the film adherence is impaired. The quantity of oxidizer is therefore to be appropriately determined, depending upon kinds thereof, so as not to incur the above described detrimental phenomena. The pH of usable plating bath is in the range of from 1.5 to 5.5. The pH, at which the precipitation of Al(OH)₃ occurs, varies depending upon the addition quantity of aluminum ions and the presence or absence of other additives. A desirable pH therefore varies accordingly. The additives, which are used in the ordinary Zn plating bath for the purpose of pH-stabilization and conductivity enhancement, may also be used as heretofore. Boric acid, ammonium chloride, citric acid, fluorides, Na₂SO₄, and the like may be added. In the foregoing descriptions, the plating is described for the ordinary pure Zn plating. However, it is likewise possible to carry out a composite plating of Zn based alloy and metallic compound. In the case of not using the oxidizer, various metallic ions such as Ti, Zr, Co, Mn, Ni, Ca, Mg, Cr, and the like are added to the bath and then deposit in a metallic state together with Zn. When the oxidizer is used, the metallic ions having the claimed valency co-deposit in the form of a compound, such as hydroxide. The metallic ions having the other valencies deposit in a metallic state. Fe, Ni, and Co deposit in a metallic state irrespective of the valency. The present invention is described in detail by way of examples. Cold-rolled sheets (SPCC) were subjected to a pre-treatment by alkali-degreasing. The cold-rolled sheets were pickled by 5% H₂SO₄, followed by water-rinsing. In the plating, the plating liquid body was stirred by means of air-blowing with the use of an air-pump. The anode used was a pure Zn sheet, while the cathode used was a test sheet (a cold-rolled sheet). In the electrolysis, the liquid temperature was 50°C, the current density was 20A/dm², the conduction time was 30 seconds and the Zn concentration was 20g/l. In Examples 1 through 4, the composite deposition of aluminum in the Zn matrix was tested. Comparative Example 1 Bath Composition Zinc sulfate heptahydrate 200g/l Sodium sulfate 100g/l Sulfuric acid 4g/l pH 3 Example 1 Bath Composition Zinc sulfate heptahydrate 200g/l Sodium sulfate 100g/l Aluminum nitrate enneahydrates 1 100g/l Sulfuric acid 4g/l pH 3 Example 2 Bath Composition Zinc sulfate heptahydrate 200g/l Sodium sulfate 100g/l Aluminum nitrate enneahydrate 3-100g/l Sulfuric acid 25g/l pH 1.8 Example 3 Bath Composition Zinc chloride 150g/l Sodium chloride 50g/l Aluminum chloride 0.5-10g/l Hydrogenborofluoride 5g/l pH 2.8 The examination of properties was carried out as follows. (1) SEM was used to investigate the presence or absence of pores so as to determine the film structure. (2) The corrosion resistance (unpainted) was investigated by the salt spray test (JIS Z2371) and the results are shown by the time until generation of red rust. (3) The corrosion resistance (E.D. sheet) was investigated by applying a 15 µm thick coating of cation electrodeposition paint (produced by Kansai Paint), then forming cross cuts on the paint coating, and subjecting the sheets to a salt spray test for 480 hours. The results are shown by the width of blister at the cut parts (maximum width at one side). 4 0 ∼ 1 mm 3 1 ∼ 3 mm 2 3 ∼ 6 mm 1 6 mm or more In addition to the above (1), the determination of film structure was carried out by the method for measuring a bulk specific gravity, which indicates the proportion of pores. The bulk specific gravity obtained was from 2 to 6.9. The specific gravity was measured by the method of; dipping a sample in 7% HCl solution for 3 minutes; measuring the weight before and after the immersion to obtain the plated weight (g/m²); obtaining a film thickness (µm) by an electromagnetic film-thickness tester; and, dividing the film weight by film thickness. The obtained results are shown in Table 1. In the following described Comparative Examples 2 and Examples 4 through 8 the deposition of metallic compound was tested with the use of an oxidizer. Comparative Example 2 Bath Composition Zinc sulfate heptahydrates 200g/l Sodium sulfate 100g/l Sulfuric acid 4g/l Comparative Example 3 Bath Composition Zinc sulfate heptahydrate 200g/l Nickel sulfate hexahydrates 100g/l Sodium sulfate 100g/l Sulfuric acid 4g/l Example 4 Bath Composition Zinc sulfate heptahydrates 200g/l Sodium sulfate 50g/l Sodium nitrate 0.5g/l Aluminum hydroxide 2.9g/l Sulfuric acid 4g/l pH 3 Example 5 Bath Composition Zinc sulfate heptahydrates 200g/l Sodium sulfate 50g/l Sodium nitrate 1.0g/l Chromium sulfate 12g/l Sulfuric acid 3g/l Example 6 Bath Composition Zinc sulfate heptahydrates 200g/l Sodium bromate 0.1g/l Aluminum hydroxide 5.8g/l Sulfuric acid 5 g/l Examle 7 Bath Composition Zinc sulfate heptahydrates 200g/l Potassium iodate 0.2g/l Cobalt sulfate heptahydrate 30g/l Sulfuric acid 5g/l Magnesium sulfate 10g/l Example 8 Bath Composition Zinc sulfate heptahydrates 200g/l Nickel sulfate hexahydrates 134g/l Hydrogen peroxide 0.2g/l Sulfuric acid 2g/l Aluminum hydroxide 2.9g/l The corrosion-resistance measured by the same method as in Table 1 is shown in Table 2. Run No. Oxidizing agent (ppm) Alloying elements (ion conc) Codepositing element (ion conc) Corrosion resistance Unpainted (hours) Cation E.D. Ex.4 NaNO₃ (500) no Al³⁺ 1g/l 180 4 Ex.5 NaNO₃ (1000) no Cr³⁺ 3g/l 70 3 Ex.6 NaBrO₃ (200) no Al³⁺ 2g/l 100 4 Ex.7 KlO₃ (200) Co²⁺ 6g/l Mg²⁺ 2g/l 130 4 Ex.8 H₂O₂ (200) Ni²⁺ 30g/l Al³⁺ 1g/l 200 4 C.Ex 2 no no no 20 1 C.Ex 3 no Ni²⁺ 56g/l no 70 3 Remarks: Ex=Example C. Ex.=Comparative Example

Claims: A Zn-based composite-plated metallic material, comprising a metallic material-substrate and, a plating layer of an electroplated Zn or Zn alloy, characterized in that a product of a cathodic precipitation-reaction on said substrate being a compound of at least one ionic metal selected from the group consisting of aluminium, calcium, magnesium, strontium, zirconium, molybdenum, chromium and tungsten, is contained in said plating layer in an amount of from 0.002 to 10% by weight in terms of said at least one metal. A Zn-based composite-plated metallic material according to claim 1, wherein said at least one ionic metal is aluminum. A Zn-based composite-plated metallic material according to claim 1 or 2, wherein said compound is one member selected from the group consisting of hydroxide, hydroxide hydrate, and phosphate. A Zn-based composite-plated metallic material according to claim 1 or 2, wherein said compound is at least one member selected from the group consisting of hydroxide, hydroxide hydrate, and oxide which is converted from said hydroxide or hydroxide hydrate. A Zn-based composite-plated metallic material according to claim 1, wherein said plating layer comprises pores. A Zn-based composite-plated metallic material according to any one of claims 1 through 5, wherein said metallic material-substrate is a steel sheet. A method for plating a Zn-based composite material on a metallic-material substrate, comprising: preparing an acidic plating solution containing Zn ions and at least one ionic metal selected from the group consisting of aluminium, calcium, magnesium, strontium, titanium, zirconium, chromium, molybdenum, and tungsten; bringing said metallic material-substrate as a cathode into contact with said plating solution; and, adjusting pH of said plating solution to such a value that, upon discharge of H⁺ and pH rise at the cathode, a compound of said at least one ionic metal is cathodically precipitated on the cathode, together with electrodeposition of said Zn ions and said plating solution further contains an oxidizer at such a concentration that said pH rise is caused mainly due to consumption of said H⁺ by said oxidizer. A method according to claim 7, wherein said at least one ionic metal is Al³⁺. A method according to claim 7, wherein said at least one ionic metal is selected from the group consisting of Mg²⁺, Sr²⁺, Ti⁴⁺, Zr⁴⁺, Cr³⁺, Mo⁶⁺ and W⁶⁺.

Inventors: MIYAWAKI, TOSHI, MORI, KAZUHIKO
Applicants: NIHON PARKERIZING CO., LTD.
Application year: 1988
Main classification: B32B15
IPC codes: C25D5, C25D15, C25D3