EP0693139B1 - Composition and process for substitutionally plating zinc or zinc-alloy surfaces - Google Patents
Composition and process for substitutionally plating zinc or zinc-alloy surfaces Download PDFInfo
- Publication number
- EP0693139B1 EP0693139B1 EP94913306A EP94913306A EP0693139B1 EP 0693139 B1 EP0693139 B1 EP 0693139B1 EP 94913306 A EP94913306 A EP 94913306A EP 94913306 A EP94913306 A EP 94913306A EP 0693139 B1 EP0693139 B1 EP 0693139B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- acid
- alloy surface
- heavy metal
- treatment
- sheet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- 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
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/32—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
-
- 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
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C22/00—Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C22/78—Pretreatment of the material to be coated
Definitions
- the present invention relates to an acidic substitutional plating bath composition, also called a "bath” herein for brevity, for application to Zn or Zn alloy surfaces, particularly to steel sheet plated with zinc-containing metal (hereinafter referred to as Zn or Zn alloy metal-plated steel sheet), and to processes for using such a composition to treat metals. More specifically, the present invention relates to an acidic substitutional plating bath composition that can be continuously employed for long periods of time while maintaining its initial performance and that, upon contact with the surface of Zn or Zn alloy metal-plated steel sheet, forms thereon a heavy metal film that contributes to the formation of a paint undercoat that is very strongly adherent for paint films.
- This acidic substitutional plating bath composition can also improve the black rust resistance of the unpainted sheet.
- Zn or Zn alloy metal-plated steel sheet encompasses steel sheet plated with zinc or a zinc alloy.
- Said zinc alloys encompass, for example, zinc-aluminum alloys, zinc-nickel alloys, and zinc-iron alloys.
- low-lead hot-dip galvanized steel sheet (with a lead content in the zinc plating layer reduced from that in conventional hot-dip galvanized steel sheet), it has already been discovered that corrosion inhibition is obtained due to the absence of lead segregation at the grain boundaries of the crystals in the plating layer and at the interface between the plating layer and alloy layer.
- Low-lead hot-dip galvanized steel sheet is, as a consequence, widely used in various industrial sectors.
- low-lead hot-dip galvanized steel sheet resists cracking during bending processes, with the result that shear stresses become concentrated in the phosphate film positioned between the steel sheet and paint film. This produces cohesive failure in the phosphate film, which in turn causes facile delamination of the paint film.
- Japanese Patent Publication Number Sho 43-12974 relates to a method in which zinciferous metal-plated steel sheet is treated with a basic aqueous solution (pH ⁇ 11) containing Co 2+ , Fe 2+ , Fe 3+ , or Ni 2+ prior to execution of a chromate treatment on the sheet.
- a basic aqueous solution pH ⁇ 11
- sludge large amounts of sludge are produced in this method due to the accumulation of the zinc ion eluting into the treatment bath with elapsed treatment time. This necessitates a sludge removal step, which impairs the workability.
- (2) Japanese Patent Publication Number Sho 52-22618 and (3) Japanese Patent Publication Number Sho 52-43171 relate to methods in which galvanized steel sheet is treated with an acidic solution (pH around 1.5) that contains Ni 2+ , Co 2+ , Fe 2+ , and/or Fe 3+ prior to execution of a chromate treatment on the sheet.
- the acidic substitutional plating baths disclosed in (2) Japanese Patent Publication Number Sho 52-22618 and (3) Japanese Patent Publication Number Sho 52-43171 contain an inorganic acid such as hydrochloric acid, sulfuric acid, hydrofluoric acid, or fluosilicic acid, or an organic acid such as citric acid, acetic acid, oxalic acid, and so forth.
- the zinc ion eluted into the plating bath is present in dissolved form through the formation of a salt with the inorganic acids or through complex formation with the organic acids.
- the pH in substitutional plating baths of this type is readily increased by the increase in zinc ion concentration, which results in a decline in the substitutional plating reactions. Due to this, large quantities of inorganic acid must be added in order to maintain the pH of the plating bath at the desired values, and this facilitates corrosion of, for example, stainless steel plating bath tanks, pipes, and so forth. Therefore such baths are quite difficult to implement on a practical basis without the use of a stainless steel reactor and piping both coated with rubber lining or the like. This use of corrosive acid, particularly a volatile one such as hydrochloric acid, also causes a deterioration in the working environment.
- Japanese Patent Application Laid Open Number Sho 61-69978 concerns a method in with low-lead hot-dip galvanized steel sheet is treated with an aqueous alkaline solution that contains Fe, Co, and/or Ni or with an aqueous hydrochloric acid solution, aqueous sulfuric acid solution, or aqueous phosphoric acid solution that contains Fe, Co, and/or Ni.
- aqueous hydrochloric acid solution, aqueous sulfuric acid solution, and aqueous alkaline solution deposition of these metals is impaired by the increase in Zn ion and increase in pH that occur with elapsed treatment time.
- chromate treatments have also been applied to zinciferous metal-plated steel sheet for the purpose of improving the corrosion resistance. While this type of treatment very effectively inhibits the development of white rust, black rust (also known as blackening) still occurs during storage and transport.
- black rust also known as blackening
- a countermeasure to this problem of post-chromating black rust consists, for example, of flash treatment by Ni, Co, or Fe as disclosed in Japanese Patent Publication Number Hei 3-49982 [49,982/1991].
- black rust inhibition is achieved by the pre-chromating treatment of Zn or Zn alloy metal-plated steel sheet with a treatment bath that has a pH of 1 to 4 or 11 to 13.5 and that contains Ni 2+ ion or Co 2+ ion. Even this method, however, suffers from a reduced workability due to the production of sludge that occurs when the zinc ion concentration becomes elevated during the course of treatment.
- the present invention seeks to introduce a very generally applicable acidic bath composition for the substitutional plating of zinciferous metal-plated steel sheet that is almost free of equipment corrosion and that is capable of a very efficient deposition of heavy metal (e.g., Ni, Co, and/ or Fe, etc.) on Zn or Zn alloy metal-plated steel sheet, with no sludge production with elapsed treatment time, uespite the increased zinc ion concentrations in the substitutional plating bath.
- heavy metal e.g., Ni, Co, and/ or Fe, etc.
- the acidic substitutional plating bath composition of the present invention for application to Zn or Zn alloy metal-plated steel sheet characteristically has a pH of 2.0 to 4.5 and consists essentially of water, 1.5 to 40 g/l as metal atoms of at least one heavy metal ion selected from nickel, iron, and cobalt; 0.5 to 10 g/l of phosphate ions, including the stoichiometric equivalent as phosphate ions of any undissociated phosphoric acid present in the solution and of all the anions other than phosphate itself produced by any degree of dissociation of phosphoric acid; 1 to 250 g/l of sulfate ions; and 1 to 20 g/l of organic acid, and optionally hydrofluoric acid, fluosilicic acid, zinc oxide or ammonia.
- the inventors have discovered that when phosphoric acid with its high pH buffering capacity is used in the acidic substitutional plating bath in place of the aforesaid inorganic acids, the pH variations are relaxed despite the increases in the zinc ion concentration, and the amount of free inorganic acid ion can therefore be restrained. This makes possible the preparation of an acidic substitutional plating bath that solves the problem with prior acidic substitutional plating baths through its almost complete lack of corrosiveness for stainless steel containers and piping.
- the plating baths disclosed in the prior-art examples referenced above contain compounds of antimony, tin, and so forth, in order to prevent a decline in the substitutional plating reactions at increased levels of zinc ion.
- the present inventors discovered that regulation of the pH to 2.0 to 4.5 and limiting the quantities of etching-active components (phosphate ions, sulfate ions, and organic acid ions) in the treatment bath to within particular ranges avoids the accumulation of large quantities of zinc ion and makes possible use of the plating bath on a continuous basis.
- the acidic substitutional plating bath in accordance with the present invention must contain the following components:
- the bath must contain at least one heavy metal ion selected from nickel, iron, and cobalt.
- the heavy metal ion selected from nickel, iron, and cobalt.
- These are advantageously supplied to the plating bath in the form of the corresponding sulfates, phosphates, carbonates, oxides, hydroxides, and organic acid salts.
- the use of nitrate is undesirable because its presence can lead to the formation of a phosphate film upon zinc dissolution.
- long-term use of the chloride runs the risk of chloride ion accumulation and corrosion of the plating equipment.
- the plating bath should contain said heavy metal ion(s) at 1.5 to 40 g/l calculated as metal atoms. Metal deposition is inadequate at below 1.5 g/l and a satisfactory effect is therefore not obtained. At above 40 g/l on the other hand, metal deposition is saturated and the economic losses due to bath carry-out become large.
- Orthophosphoric acid is preferably used as the source for the phosphate ion used by the present invention.
- the content of phosphoric acid in the plating bath should be 0.5 to 10 g/l as phosphate ion.
- the use of less than 0.5 g/l will result in a sharp increase in bath pH, which influences the component balance.
- the pH buffering activity is substantially saturated at above 10 g/l while the amount of zinc etching is increased, with a corresponding decline in deposition efficiency.
- Sulfate ions in the present invention are preferably supplied by sulfuric acid. Its content gradually increases because it is generated ⁇ by zinc ion capture ⁇ in correspondence to the increase in zinc ion. Accordingly, the sulfate ion concentration should be determined by the amount of zinc etching and the amount of plating bath carry-out, but must generally fall in the range of 1 to 250 g/l. Capture of the eluted zinc ion is inadequate at below 1 g/l, while exceeding 250 g/l is economically unattractive because the effect is saturated at such levels.
- the organic acid used by the present invention comprises at least one selection from glycolic acid, lactic acid, malic acid, tartaric acid, citric acid, gluconic acid, and ascorbic acid.
- the organic acid is citric or malic acid.
- the organic acid concentration should be 1 to 20 g/l. Both the ability to capture eluted zinc and the pH buffering capacity are inadequate when the organic acid concentration is less than 1 g/l. On the other hand, the effect becomes saturated when the organic acid concentration exceeds 20 g/l and these high concentrations also impair the heavy metal deposition efficiency.
- An acidic substitutional plating bath in accordance with the present invention consisting of the ingredients as described above should have a pH adjusted into the range of 2.0 to 4.5.
- the pH value may be maintained in this range through the supplementary addition of hydrofluoric acid or fluosilicic acid to the plating bath.
- Zinc oxide or ammonia can be added when the pH is too low.
- the reasons for the restriction to the pH range of 2.0 to 4.5 are as follows: a pH below 2 signifies an excessive content of inorganic acid, which results in too much zinc etching; equipment corrosion also becomes a risk at lower pH values; at pH values in excess of 4.5 the substitutional plating reactivity is impaired when the amount of eluted zinc ion has become increased.
- Acidic substitutional plating may be run by bringing the surface of the Zn or Zn alloy metal-plated steel sheet into contact with the acidic substitutional plating bath by spraying, immersion, coating, and so forth. Plating is thereby conducted to the desired degree, and is followed by a water wash and drying.
- the temperature of the plating bath should be room temperature to 80° C, and a treatment time of less than 1 minute will be sufficient. Insofar as concerns the amount of heavy metal deposition, 1 to 100 mg/m 2 can provide a desirable performance in the case of paint undercoating treatments, while 0.3 to 20 mg/m 2 can provide a desirable black rust prevention in the case of anticorrosion chromate treatments.
- the desired effects may not appear when the amount of heavy metal does not meet these lower limits, while exceeding the upper limits is economically unattractive because no additional improvement in performance is obtained above the upper limits.
- Simply driving off the water is sufficient for drying, and the sheet temperature in drying will generally fall in the range of 50° C to 100° C.
- the substitutional plating bath in accordance with the present invention may be applied to the surface of pure zinc, hot-dip galvanization, hot-dip galvanization that contains aluminum or iron as alloying components, and steel sheet electroplated with zinc or Zn or Zn alloy metal.
- the Zn or Zn alloy metal-plated steel sheet is typically subjected to an application-type chromate treatment for the purpose of improving the corrosion resistance, and this is followed by painting.
- the execution of the subject surface treatment imparts a microscopically etched texture to the surface of the Zn or Zn alloy metal-plated steel sheet which has an anchoring effect on the paint film.
- test sheets [as described in General Condition (1) below] were substitutionally plated using a treatment bath with the composition reported in Table 1.
- the organic acid was citric acid in Examples 1 - 6 and malic acid in Examples 7 - 12.
- the substitutionally plated test sheets and test sheet without substitutional plating (Comparison Example 4) were then cleaned, dried, chromated, and painted in this sequence as described in (3) through (6) below.
- the painted test sheets were subsequently submitted to flexural testing and corrosion resistance testing as described in (7) and (8) below.
- Table 2 reports the following values: the substitutional plating conditions, the presence/absence of sludge production and the amount of zinc ion in the bath for treatment bath into which zinc ion has been dissolved by the continuous treatment of test sheets, the amount of heavy metal deposition by substitutional plating, and the results of flexural testing and corrosion resistance testing on the painted sheet.
- test sheets as reported in (1) below were subjected to substitutional plating treatments using the treatment bath compositions reported in Table 3.
- the substitutionally plated test sheets and test sheet without substitutional plating (Comparison Example 8) were then cleaned, dried, chromated, and painted in this sequence as described in (3) through (6) below.
- Comparison Example 7 the test sheet was treated with zinc phosphate and then painted. The painted test sheets were subsequently submitted to flexural testing and edge creepage testing as described in (7) and (8) below.
- Table 4 reports the following values: the substitutional plating conditions, the presence/absence of sludge production and the amount of zinc ion in the bath for treatment bath into which zinc ion has been dissolved by the continuous treatment of test sheet, the amount of heavy metal deposition by substitutional plating, and the results of flexural testing and edge creepage testing on the painted sheet.
- test sheets as reported in (1) below were subjected to substitutional plating treatments using the treatment bath compositions reported in Table 5.
- the substitutionally plated test sheets and test sheet without substitutional plating (Comparison Example 11) were then degreased, cleaned, dried, chromated, and painted in this sequence as described in (2) through (9) below.
- the thus-treated test sheets were subsequently submitted to adherence testing on the painted sheet and corrosion resistance testing on the painted sheet as described in (10) and (11) below.
- test sheets as reported in (1) below were subjected to substitutional plating treatments using the treatment bath compositions reported in Table 7.
- the substitutionally plated test sheets and test sheet without substitutional plating (Comparison Example 14) were then cleaned, dried, and chromated in this sequence as described in (3) through (5) below.
- the thus-treated test sheets were subsequently submitted to accelerated white rust testing and accelerated black rust testing as described in (6) and (7) below.
- Table 8 reports the following values: the substitutional plating conditions, the presence/absence of sludge production and the amount of zinc ion in the bath for treatment bath into which zinc ion has been dissolved by the continuous treatment of test sheet, the amount of heavy metal deposition by substitutional plating, and the results of accelerated white rust testing and accelerated black rust testing.
- the acidic substitutional plating bath composition of the invention for zinciferous metal-plated steel sheet imparts an excellent adherence and corrosion resistance to the painted sheet.
- this composition yields an excellent black rust resistance.
- the acidic substitutional plating bath composition of the invention retains its initial performance for long periods of time and can therefore be used on a continuous basis. Finally, it is almost completely free of corrosiveness for equipment.
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Treatment Of Metals (AREA)
- Chemically Coating (AREA)
- Electroplating And Plating Baths Therefor (AREA)
- Electroplating Methods And Accessories (AREA)
Abstract
Description
As used herein, the term "Zn or Zn alloy metal-plated steel sheet" encompasses steel sheet plated with zinc or a zinc alloy. Said zinc alloys encompass, for example, zinc-aluminum alloys, zinc-nickel alloys, and zinc-iron alloys.
Example ("E") and Comparison Example ("CE") Numbers | Treatment Composition Characteristics | ||||||||
g/ℓ in the Composition of: | PH | ||||||||
Zn | Ni | Fe | Co | PO4 -3 | SO4 -2 | OA | Other | ||
E 1.1 | 0 | - | - | 2.0 | 1.5 | 4 | 1.5 | - | 2.4 |
E 1.2 | 25 | - | - | 2.0 | 1.5 | 38 | 1.6 | - | 2.4 |
E 1.3 | 50 | - | - | 2.1 | 1.6 | 79 | 1.6 | - | 2.5 |
E 2.1 | 5 | 30 | - | - | 4.0 | 49 | 3.0 | ZnO | 3.5 |
E 2.2 | 25 | 30 | - | - | 4.1 | 81 | 3.0 | - | 3.5 |
E 2.3 | 50 | 30 | - | - | 4.0 | 122 | 2.9 | - | 3.5 |
E 3.1 | 2 | - | 6.8 | - | 2.2 | 5 | 9.1 | 0.5 F- | 2.1 |
E 3.2 | 15 | - | 6.7 | - | 2.1 | 27 | 9.0 | 0.5 F- | 2.2 |
E 3.3 | 30 | - | 7.0 | - | 2.3 | 48 | 9.1 | 0.5 F- | 2.1 |
CE 1.1 | 0 | - | - | 2.0 | - | 10 | 1.5 | - | 2.4 |
CE 1.2 | 5 | - | - | 2.0 | - | 25 | 1.5 | - | 3.8 |
CE 1.3 | 10 | - | - | 2.0 | - | 50 | 1.6 | - | 4.9 |
CE 2.1 | 0 | - | 3.7 | 2.4 | - | - | - | - | 13.2 |
CE 2.2 | 5 | - | 3.7 | 2.5 | - | - | - | - | 13.1 |
CE 2.3 | 10 | - | 2.8 | 1.6 | - | - | - | - | 13.1 |
CE 3.1 | 0 | 5.9 | - | - | 48 | 6.5 | - | - | 1.8 |
CE 3.2 | 5 | 5.9 | - | - | 48 | 7.7 | - | - | 2.0 |
CE 3.3 | 8 | 5.0 | - | - | 29 | 8.4 | - | - | 2.1 |
CE 4 | No substitutional plating |
Example ("E") and Comparison Example ("CE") Numbers | Sludge Production in the Treatment Bath? | Conditions of Treatment | AOM, mg/m2 | FTR | CTR | ||
Type | °C | Sec | |||||
E 1.1 | no | spray | 65 | 7 | 18 | 5 | NA |
E 1.2 | no | spray | 65 | 7 | 18 | 5 | NA |
E 1.3 | no | spray | 65 | 7 | 17 | 5 | NA |
E 2.1 | no | dip | 50 | 10 | 22 | 5 | NA |
E 2.2 | no | dip | 50 | 10 | 21 | 5 | NA |
E 2.3 | no | dip | 50 | 10 | 20 | 5 | NA |
E 3.1 | no | dip | 45 | 5 | 8 | 5 | NA |
E 3.2 | no | dip | 45 | 5 | 7 | 4 | NA |
E 3.3 | no | dip | 45 | 5 | 8 | 5 | NA |
CE 1.1 | no | spray | 50 | 12 | 8 | 5 | NA |
CE 1.2 | no | spray | 50 | 12 | 1.0 | 2 | NA |
CE 1.3 | yes | spray | 50 | 12 | 0.2 | 1 | NA |
CE 2.1 | no | spray | 70 | 30 | 35 | 5 | 9F |
CE 2.2 | no | spray | 70 | 30 | 10 | 4 | 8M |
CE 2.3 | yes | spray | 70 | 30 | - | - | - |
CE 3.1 | no | spray | 50 | 8 | 11 | 4 | NA |
CE 3.2 | no | spray | 50 | 8 | 0.5 | 1 | 7M |
CE 3.3 | yes | spray | 50 | 8 | - | - | - |
CE 4 | none | - | 1 | NA | |||
Notes for Table 2 "AOM" = add-on mass of heavy metal achieved by the substitutional plating; "FTR" = flexural test results for painted, treated sheets after a 2 T bend; "CTR" = corrosion resistance test results for painted, treated sheets; "Sec" = seconds of treatment time; "NA" = no abnormalities. |
Example ("E") and Comparison Example ("CE") Numbers | Treatment Composition Characteristics | ||||||||
g/ℓ in the Composition of: | PH | ||||||||
Zn | Ni | Fe | Co | PO4 -3 | SO4 -2 | OA | Other | ||
E 4.1 | 0 | 4.5 | - | 2.0 | 5.1 | 11 | 2.9 | - | 2.8 |
E 4.2 | 25 | 4.5 | - | 2.1 | 5.2 | 43 | 2.8 | - | 2.9 |
E 4.3 | 50 | 4.6 | - | 2.1 | 5.1 | 70 | 2.9 | - | 3.0 |
E 5.1 | 5 | - | 35 | - | 0.8 | 63 | 1.3 | 1.6 F- | 2.4 |
E 5.2 | 50 | - | 35 | - | 0.8 | 140 | 1.4 | 1.6 F- | 2.4 |
E 5.3 | 100 | - | 35 | - | 0.8 | 210 | 1.4 | 1.5 F- | 2.4 |
E 6.1 | 0 | 9.9 | - | - | 8.6 | 2 | 8 | NH3 | 3.8 |
E 6.2 | 25 | 9.9 | - | - | 8.7 | 38 | 8 | - | 3.9 |
E 6.3 | 50 | 10.0 | - | - | 8.7 | 82 | 9 | - | 4.0 |
CE 5.1 | 0 | 4.5 | - | 2.0 | 5.1 | 1.9 | 10 | 9.4 NO3 - | 2.6 |
CE 5.2 | 5 | 4.5 | - | 2.0 | 5.1 | 2.0 | 9 | 9.9 NO3 - | 2.5 |
CE 6.1 | 0 | - | 35 | - | 11 | 60 | 10.0 | 1.6 F- | 1.4 |
CE 6.2 | 50 | - | 34 | - | 11 | 63 | 9.9 | 1.6 F- | 1.6 |
CE 6.3 | 100 | - | 34 | - | 12 | 68 | 10.1 | 1.7 F- | 1.8 |
CE 7 | Zinc phosphate conversion coating of 1 g/m2 | ||||||||
CE 8 | No substitutional plating or other coating before painting | ||||||||
Note for Table 3 "OA" = Organic Acid. |
Example ("E") and Comparison Example ("CE") Numbers | Sludge Production in the Treatment Bath? | Conditions of Treatment | AOM, mg/m2 | FTR | ECT, mm | ||
Type | °C | Sec | |||||
E 4.1 | no | dip | 55 | 10 | 35 | 5 | 5 |
E 4.2 | no | dip | 55 | 10 | 33 | 5 | 6 |
E 4.3 | no | dip | 55 | 10 | 33 | 5 | 5 |
E 5. | no | dip | 75 | 5 | 65 | 5 | 5 |
E 5.2 | no | dip | 75 | 5 | 65 | 5 | 5 |
E 5.3 | no | dip | 75 | 5 | 64 | 5 | 5 |
E 6.1 | no | spray | 60 | 8 | 29 | 5 | 6 |
E 6.2 | no | spray | 60 | 8 | 28 | 5 | 6 |
E 6.3 | no | spray | 60 | 8 | 29 | 4 | 7 |
CE 5.1 | no | dip | 45 | 8 | 19 | 5 | 7 |
CE 5.2 | no | dip | 45 | 8 | 15* | 2 | 5 |
CE 6.1 | no | spray | 50 | 10 | 24 | 5 | 6 |
CE 6.2 | no | spray | 50 | 10 | 4 | 4 | 9 |
CE 6.3 | yes | spray | 50 | 10 | 0.2 | 1 | 16 |
CE 7 | not applicable | - | 1 | 5 | |||
CE 8 | none | - | 1 | 20 | |||
Notes for Table 4 "AOM" = add-on mass of heavy metal achieved by the substitutional plating; "Sec" =seconds of treatment time; "FTR" = flexural test results for painted, treated sheets after a 2 T bend; "ECT" = edge creepage results for painted, treated sheets. |
Example ("E") and Comparison Example ("CE") Numbers | Treatment Composition Characteristics | ||||||||
g/ℓ in the Composition of: | PH | ||||||||
Zn | Ni | Fe | Co | PO4 -3 | SO4 -2 | OA | Other | ||
E 7.1 | 0 | - | 1.0 | 1.4 | 2.9 | 19 | 4.9 | - | 3.0 |
E 7.2 | 25 | - | 1.0 | 1.4 | 2.8 | 37 | 5.0 | - | 3.1 |
E 7.3 | 50 | - | 0.9 | 1.4 | 2.8 | 73 | 5.0 | - | 3.0 |
E 8.1 | 0 | 3.1 | - | - | 5.1 | 5 | 3.5 | - | 2.5 |
E 8.2 | 25 | 3.1 | - | - | 5.0 | 32 | 3.5 | - | 2.5 |
E 8.3 | 50 | 3.2 | - | - | 5.2 | 69 | 3.5 | - | 2.5 |
E 9.1 | 5 | 35 | - | - | 4.7 | 64 | 2.1 | 1.8 F- | 4.2 |
E 9.2 | 50 | 35 | - | - | 4.6 | 101 | 2.0 | 1.8 F- | 4.2 |
E 9.3 | 100 | 35 | - | - | 4.5 | 145 | 2.0 | 1.7 F- | 4.3 |
CE 9.1 | 0 | - | 1.0 | 1.4 | 2.9 | 19 | - | - | 3.3 |
CE 9.2 | 10 | - | 1.0 | 1.4 | 2.9 | 27 | - | - | 3.9 |
CE 9.3 | 25 | - | 1.0 | 1.4 | 2.8 | 35 | - | - | 5.0 |
CE 10.1 | 0 | - | 0.8 | 0.4 | 2.9 | 19 | 4 | - | 3.0 |
CE 10.2 | 5 | - | 0.8 | 0.4 | 2.9 | 22 | 4 | - | 3.0 |
CE 11 | No substitutional plating or other coating before painting | ||||||||
Note for Table 5 "OA" = Organic Acid. |
Example ("E") and Comparison Example ("CE") Numbers | Sludge Production in the Treatment Bath? | Conditions of Treatment | AOM, mg/m2 | Adherence Test Results | mm CR | |||
Type | °C | Sec | CT | ET | ||||
E 7.1 | no | spray | 70 | 8 | 25 | 4 | 4 | 0.2 |
E 7.2 | no | spray | 70 | 8 | 24 | 4 | 3 | 0.2 |
E 7.3 | no | spray | 70 | 8 | 24 | 4 | 4 | 0.2 |
E 8.1 | no | dip | 70 | 10 | 34 | 4 | 4 | 0.2 |
E 8.2 | no | dip | 70 | 10 | 36 | 4 | 4 | 0.2 |
E 8.3 | no | dip | 70 | 10 | 35 | 4 | 3 | 0.2 |
E 9.1 | no | spray | 60 | 5 | 14 | 4 | 4 | 0.5 |
E 9.2 | no | spray | 60 | 5 | 15 | 4 | 4 | 0.2 |
E 9.3 | no | spray | 60 | 5 | 15 | 4 | 4 | 0.5 |
CE 9.1 | no | spray | 60 | 10 | 17 | 4 | 3 | 0.2 |
CE 9.2 | no | spray | 60 | 10 | 7 | 4 | 3 | 0.2 |
CE 9.3 | yes | spray | 60 | 10 | 0.2 | 2 | 1 | 1.0 |
CE 10.1 | no | spray | 70 | 30 | 10 | 4 | 4 | 0.2 |
CE 10.2 | no | spray | 70 | 30 | 0.5 | 2 | 2 | 1.0 |
CE 11 | none | - | 1 | 1.5 | ||||
Notes for Table 6 "Sec" = seconds of treatment time; "AOM" = add-on mass of heavy metal achieved by the substitutional plating; "CR" = corrosion resistance results for painted, treated sheets; "CT' = checkerboard test; "ET" = Erichsen test. |
Example ("E") and Comparison Example ("E") Numbers | Treatment Composition Characteristics | ||||||||
g/ℓ in the Composition of: | pH | ||||||||
Zn | Ni | Fe | Co | PO4 -3 | SO4 -2 | OA | Other | ||
E 10.1 | 2 | 0.8 | 1.0 | - | 1.0 | 3 | 1.2 | ZnCO3 | 4.0 |
E 10.2 | 10 | 0.9 | 1.0 | - | 0.9 | 15 | 1.2 | 4.1 | |
E 10.3 | 25 | 0.8 | 1.0 | - | 0.9 | 38 | 1.2 | 4.0 | |
E 11.1 | 5 | 3.0 | - | - | 4.0 | 9 | 3.0 | 3.2 | |
E 11.2 | 25 | 3.0 | - | - | 4.1 | 41 | 3.0 | 3.2 | |
E 11.3 | 50 | 3.0 | - | - | 4.0 | 75 | 2.9 | 3.2 | |
E 12.1 | 2 | - | - | 16 | 2.5 | 5 | 9.1 | NH3 | 2.8 |
E 12.2 | 15 | - | - | 16 | 2.6 | 27 | 9.0 | 2.7 | |
E 12.3 | 30 | - | - | 16 | 2.6 | 48 | 9.1 | 2.8 | |
CE 12.1 | 0 | 11 | - | - | - | 19 | - | 2.0 | |
CE 12.2 | 5 | 10 | - | - | - | 30 | - | 1.5 | |
CE 12.3 | 10 | 10 | - | - | - | 52 | - | 1.0 | |
CE 13.1 | 0 | - | - | 11 | - | 17 | 15 | 13.2 | |
CE 13.2 | 5 | - | - | 11 | - | 18 | 15 | 13.1 | |
CE 13.3 | 10 | - | - | 9 | - | 18 | 15 | 13.1 | |
CE 14 | No substitutional plating |
Example ("E") and Comparison Example ("CE") Numbers | Sludge Production in the Treatment Bath? | Conditions of Treatment | AOM, mg/m2 | RWR | RBR | ||
Type | °C | Sec | |||||
E 10.1 | no | spray | 45 | 3 | 1.7 | 5 | 5 |
E 10.2 | no | spray | 45 | 3 | 1.6 | 5 | 5 |
E 10.3 | no | spray | 45 | 3 | 1.5 | 5 | 5 |
E 11.1 | no | dip | 60 | 5 | 2.5 | 5 | 5 |
E 11.2 | no | dip | 60 | 5 | 2.5 | 5 | 5 |
E 11.3 | no | dip | 60 | 5 | 2.4 | 5 | 5 |
E 12.1 | no | dip | 50 | 5 | 2.9 | 5 | 5 |
E 12.2 | no | dip | 50 | 5 | 2.8 | 5 | 5 |
E 12.3 | no | dip | 50 | 5 | 2.9 | 5 | 5 |
CE 12.1 | no | dip | 50 | 10 | 23.9 | 1 | 5 |
CE 12.2 | no | dip | 50 | 10 | 5.0 | 4 | 5 |
CE 12.3 | no | dip | 50 | 10 | 0.1 | 5 | 2 |
CE 13.1 | no | dip | 60 | 2 | 2.4 | 5 | 5 |
CE 13.2 | no | dip | 60 | 2 | 2.4 | 5 | 5 |
CE 13.3 | yes | dip | 60 | 2 | 2.2 | 5 | 5 |
CE 14 | none | - | 5 | 1 | |||
Notes for Table 8 "AOM" = add-on mass of heavy metal achieved by the substitutional plating; "RWR" = resistance to white rusting test results for painted, treated sheets; "RBR" = resistance to black rusting test results for painted, treated sheets; "Sec" = seconds of treatment time. |
Claims (7)
- An aqueous substitutional plating bath composition having a pH of 2.0 to 4.5 and consisting essentially of water;(A) from 1.5 to 40 g/l as metal atom of heavy metal ions selected from the group consisting of nickel, iron, cobalt, and mixtures of any two or more thereof;(B) from 0.5 to 10 g/l of phosphate ions;(C) from 1 to 250 g/l of sulfate ions; and(D) from 1 to 20 g/l of organic acid and optionally hydrofluoric acid, fluosilicic acid, zinc oxide or ammonia.
- The aqueous composition in accordance with claim 1 in which the organic acid is selected from the group consisting of glycolic acid, lactic acid, malic acid, tartaric acid, citric acid, gluconic acid, ascorbic acid, and mixtures of any two or more thereof.
- The aqueous composition in accordance with claim 1 or 2 comprising at least one of hydrofluoric acid, fluosilicic acid, zinc oxide or ammonia.
- A process of comprising steps of contacting a Zn or Zn alloy surface with a composition according to anyone of claims 1 to 3 for a time sufficient to deposit on the Zn or Zn alloy surface at least 0.3 mg of heavy metal per square meter of Zn or Zn alloy surface contacted, removing the Zn or Zn alloy surface from contact with the aqueous composition according to anyone of claims 1 to 3, washing the coating of heavy metal on the Zn or Zn alloy surface with water, and drying the Zn or Zn alloy surface.
- A process according to claim 4, wherein the amount of heavy metal deposited on the Zn or Zn alloy surface is from 1 to 100 mg/m2 and the dried Zn or Zn alloy surface is subsequently painted.
- A process according to claim 4, wherein the amount of heavy metal deposited on the Zn or Zn alloy surface is from 0.3 to 20 mg/m2, and the dried Zn or Zn alloy surface is subsequently subjected to an anticorrosion chromate treatment.
- A process according to anyone of claims 4 to 6, wherein Zn or Zn alloy surface is that of Zn or Zn alloy metal plated steel sheet.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5080883A JP2968147B2 (en) | 1993-04-07 | 1993-04-07 | Acid displacement plating solution composition for zinc-containing metal plated steel sheet |
JP80883/93 | 1993-04-07 | ||
PCT/US1994/003225 WO1994023089A1 (en) | 1993-04-07 | 1994-03-28 | Composition and process for substitutionally plating zinciferous surfaces |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0693139A1 EP0693139A1 (en) | 1996-01-24 |
EP0693139A4 EP0693139A4 (en) | 1996-02-07 |
EP0693139B1 true EP0693139B1 (en) | 1998-07-22 |
Family
ID=13730748
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94913306A Expired - Lifetime EP0693139B1 (en) | 1993-04-07 | 1994-03-28 | Composition and process for substitutionally plating zinc or zinc-alloy surfaces |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0693139B1 (en) |
JP (1) | JP2968147B2 (en) |
CN (1) | CN1065574C (en) |
AT (1) | ATE168728T1 (en) |
CA (1) | CA2158856A1 (en) |
DE (1) | DE69411902T2 (en) |
TW (1) | TW301675B (en) |
WO (1) | WO1994023089A1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5463609B2 (en) * | 2005-03-31 | 2014-04-09 | Jfeスチール株式会社 | Chrome-free surface-treated galvanized steel sheet, method for producing the same, and surface treatment liquid |
JP2007023353A (en) * | 2005-07-19 | 2007-02-01 | Yuken Industry Co Ltd | Non-chromium reactive chemical conversion treatment of galvanized member |
DE102006051384A1 (en) | 2006-10-27 | 2008-04-30 | Seppeler Holding Und Verwaltungs Gmbh & Co. Kg | Process for the pre-weathering of metal parts with a predominantly zinc surface |
DE102007021364A1 (en) * | 2007-05-04 | 2008-11-06 | Henkel Ag & Co. Kgaa | Metallizing pretreatment of zinc surfaces |
CN101311308B (en) * | 2007-05-24 | 2011-04-27 | 西北工业大学 | Five-component alloy plating solution for chemical plating on surface of fiberglass and method for preparing same |
US9528187B2 (en) | 2010-09-15 | 2016-12-27 | Jfe Steel Corporation | Steel sheet for containers and manufacturing method for same |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3515600A (en) * | 1966-10-19 | 1970-06-02 | Hooker Chemical Corp | Metal treating process and composition |
JPS5222618B2 (en) * | 1972-11-06 | 1977-06-18 | ||
DE2543523A1 (en) * | 1975-09-30 | 1977-04-07 | Metallgesellschaft Ag | DUST LOCK |
FR2531103B1 (en) * | 1982-07-30 | 1985-11-22 | Onera (Off Nat Aerospatiale) | BATH FOR CHEMICAL DEPOSITION OF NICKEL AND / OR COBALT USING A REDUCER BASED ON BORON OR PHOSPHORUS |
JPS60248882A (en) * | 1984-05-24 | 1985-12-09 | Aisin Seiki Co Ltd | Electroless plating bath for plating high-phosphorus nickel alloy |
FR2569203B1 (en) * | 1984-08-16 | 1989-12-22 | Produits Ind Cie Fse | PROCESS FOR THE TREATMENT BY CHEMICAL CONVERSION OF SUBSTRATES IN ZINC OR IN ONE OF ITS ALLOYS, CONCENTRATE AND BATH USED FOR THE IMPLEMENTATION OF THIS PROCESS |
JPS6169978A (en) * | 1984-09-12 | 1986-04-10 | Nisshin Steel Co Ltd | Pretreatment for low-lead galvanized steel sheet before coating |
GB8507181D0 (en) * | 1985-03-20 | 1985-04-24 | Omi International Benelux Bv | Passivation |
JPH0696773B2 (en) * | 1989-06-15 | 1994-11-30 | 日本ペイント株式会社 | Method for forming zinc phosphate film on metal surface |
FR2654440B1 (en) * | 1989-11-16 | 1993-07-30 | Produits Ind Cie Fse | PROCESS FOR THE CHEMICAL CONVERSION OF METAL SUBSTRATES, BATH USED IN THIS PROCESS AND CONCENTRATE FOR THE PREPARATION OF THE BATH. |
JP2586688B2 (en) * | 1990-05-07 | 1997-03-05 | 上村工業株式会社 | Electroplating method of glass-metal composite |
US5258061A (en) * | 1992-11-20 | 1993-11-02 | Monsanto Company | Electroless nickel plating baths |
-
1993
- 1993-04-07 JP JP5080883A patent/JP2968147B2/en not_active Expired - Fee Related
-
1994
- 1994-03-28 CA CA002158856A patent/CA2158856A1/en not_active Abandoned
- 1994-03-28 EP EP94913306A patent/EP0693139B1/en not_active Expired - Lifetime
- 1994-03-28 WO PCT/US1994/003225 patent/WO1994023089A1/en active IP Right Grant
- 1994-03-28 DE DE69411902T patent/DE69411902T2/en not_active Expired - Fee Related
- 1994-03-28 AT AT94913306T patent/ATE168728T1/en not_active IP Right Cessation
- 1994-03-31 TW TW083102839A patent/TW301675B/zh active
- 1994-04-07 CN CN94104596A patent/CN1065574C/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2968147B2 (en) | 1999-10-25 |
EP0693139A4 (en) | 1996-02-07 |
ATE168728T1 (en) | 1998-08-15 |
JPH06293973A (en) | 1994-10-21 |
CN1065574C (en) | 2001-05-09 |
CA2158856A1 (en) | 1994-10-13 |
CN1093415A (en) | 1994-10-12 |
DE69411902T2 (en) | 1999-04-08 |
WO1994023089A1 (en) | 1994-10-13 |
TW301675B (en) | 1997-04-01 |
DE69411902D1 (en) | 1998-08-27 |
EP0693139A1 (en) | 1996-01-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2010001861A1 (en) | Chemical conversion liquid for metal structure and surface treating method | |
AU2020200A (en) | Composition and process for treating metal surfaces | |
EP0545993B1 (en) | Composition and method for chromating treatment of metal | |
WO2006098359A1 (en) | Surface-treated metallic material | |
JP4312583B2 (en) | Painted Zn-Al alloy plated steel sheet with excellent corrosion resistance | |
JP3851482B2 (en) | Galvanized steel sheet with excellent white rust resistance and coating adhesion | |
EP0693139B1 (en) | Composition and process for substitutionally plating zinc or zinc-alloy surfaces | |
US5624480A (en) | Composition and process for substitutionally plating zinciferous surfaces | |
JP4312635B2 (en) | Painted aluminized steel sheet with excellent corrosion resistance | |
JP3288152B2 (en) | Method for producing galvanized steel sheet with excellent resistance to blackening and white rust | |
JP2968127B2 (en) | Acid displacement plating solution for zinc or galvanized steel sheet | |
JP4795647B2 (en) | Galvanized steel sheet with excellent corrosion resistance, paintability and adhesion | |
JP2904592B2 (en) | Pretreatment method for chromate treatment of zinc or zinc alloy | |
US6461449B1 (en) | Conversion coating zinciferous surfaces to resist blackening and white rust | |
EP0553271B1 (en) | Preatment for zinc and zinc alloys prior to chromating | |
JP2901341B2 (en) | Pretreatment method for chromate treatment of zinc or zinc alloy | |
JPH09228067A (en) | Surface treated steel sheet excellent in resistance against environmental pollution and corrosion | |
JP3137434B2 (en) | Method for producing galvanized steel sheet with excellent resistance to blackening and white rust | |
JPH1036972A (en) | Acidic substitution plating liquid for zinc-containing metal plated steel sheet | |
JP2004238699A (en) | Surface-conditioning method, non-chromium coated original sheet and production method of non-chromium coated steel sheet | |
JPH0711454A (en) | Method for chromating metal by coating | |
JPH057477B2 (en) | ||
JPH0774461B2 (en) | Surface treatment method of zinc or zinc alloy | |
JPH05195249A (en) | Pretreatment for chromate treatment of galvanized steel sheet | |
JPH06346250A (en) | Coating type chromating method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19951002 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE DE ES FR GB IT SE |
|
A4 | Supplementary search report drawn up and despatched |
Effective date: 19951221 |
|
AK | Designated contracting states |
Kind code of ref document: A4 Designated state(s): AT BE DE ES FR GB IT SE |
|
17Q | First examination report despatched |
Effective date: 19970401 |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE DE ES FR GB IT SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY Effective date: 19980722 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19980722 |
|
REF | Corresponds to: |
Ref document number: 168728 Country of ref document: AT Date of ref document: 19980815 Kind code of ref document: T |
|
ITF | It: translation for a ep patent filed |
Owner name: JACOBACCI & PERANI S.P.A. |
|
REF | Corresponds to: |
Ref document number: 69411902 Country of ref document: DE Date of ref document: 19980827 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 19981022 |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20000302 Year of fee payment: 7 Ref country code: FR Payment date: 20000302 Year of fee payment: 7 Ref country code: DE Payment date: 20000302 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20000328 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010328 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010331 |
|
BERE | Be: lapsed |
Owner name: HENKEL CORP. Effective date: 20010331 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20010328 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20011130 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20020101 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20050328 |