EP0414301B1 - Verfahren zur Erzeugung von Phosphatüberzügen auf Metalloberflächen - Google Patents

Verfahren zur Erzeugung von Phosphatüberzügen auf Metalloberflächen Download PDF

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Publication number
EP0414301B1
EP0414301B1 EP90202148A EP90202148A EP0414301B1 EP 0414301 B1 EP0414301 B1 EP 0414301B1 EP 90202148 A EP90202148 A EP 90202148A EP 90202148 A EP90202148 A EP 90202148A EP 0414301 B1 EP0414301 B1 EP 0414301B1
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EP
European Patent Office
Prior art keywords
phosphating
water
bath
rinsing
phosphate
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
Application number
EP90202148A
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German (de)
English (en)
French (fr)
Other versions
EP0414301A1 (de
Inventor
Georg Blümlhuber
Horst Dr. Gehmecker
Dieter Hauffe
Lothar Dr. Kaul
Thomas Nitschke
Werner Dr. Rausch
Hardy Wietzoreck
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chemetall GmbH
Original Assignee
Metallgesellschaft AG
Continentale Parker Ste
Continentale Parker SA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Metallgesellschaft AG, Continentale Parker Ste, Continentale Parker SA filed Critical Metallgesellschaft AG
Priority to AT90202148T priority Critical patent/ATE85987T1/de
Publication of EP0414301A1 publication Critical patent/EP0414301A1/de
Application granted granted Critical
Publication of EP0414301B1 publication Critical patent/EP0414301B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/18Orthophosphates containing manganese cations
    • C23C22/182Orthophosphates containing manganese cations containing also zinc cations
    • C23C22/184Orthophosphates containing manganese cations containing also zinc cations containing also nickel cations
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/12Orthophosphates containing zinc cations
    • C23C22/13Orthophosphates containing zinc cations containing also nitrate or nitrite anions
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/07Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
    • C23C22/08Orthophosphates
    • C23C22/22Orthophosphates containing alkaline earth metal cations
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/05Chemical 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 using aqueous solutions
    • C23C22/06Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/36Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
    • C23C22/362Chemical 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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing also zinc cations
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C22/00Chemical 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
    • C23C22/73Chemical 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 characterised by the process

Definitions

  • the invention relates to a wastewater-free method for producing phosphate coatings on metal surfaces by means of aqueous zinc phosphate solutions containing iron (II) and nitrate ions.
  • the process of producing phosphate coatings by means of aqueous zinc phosphate solutions is widely used in the metalworking industry.
  • the phosphate layers produced on the treated metal surfaces with this process are used in particular to facilitate sliding and non-cutting cold forming, as well as for corrosion protection and as a paint primer.
  • Such phosphating baths usually have a pH between about 1.8 and 3.8 and contain zinc and phosphate ions as process-determining components.
  • other cations e.g. Ammonium, calcium, cobalt, iron, potassium, copper, sodium, magnesium, manganese, may be present.
  • the phosphating baths are generally oxidizing agents, e.g. Bromate, chlorate, nitrate, nitrite, organic nitro compounds, perborate, persulfate, hydrogen peroxide, added. Oxygen-containing gas can also be used for the oxidation of iron (II) to iron (III).
  • additives such as Fluoride, silicon fluoride, boron fluoride, citrate and tartrate. Due to the large number of individual components and their possible combinations, there are a large number of different phosphating bath compositions.
  • the phosphating baths are usually brought into contact with the workpiece surfaces to be treated in immersion, flooding or spraying. During the contact period between a few seconds up to half an hour and more, crystalline phosphate layers are firmly integrated by chemical reaction with the metal. Since residues of the phosphating solution remaining on the surface usually interfere with further processing, the water is thoroughly rinsed after the phosphating. In order to avoid harmful accumulation of the ingredients of the phosphating bath in the rinsing baths, these are operated with an inflow of fresh water and an overflow of contaminated rinsing water. The contaminated rinsing water contains environmentally hazardous substances and therefore requires special treatment before it can be discharged into the sewage system or a drain.
  • a method is known from DE-A-2538347 in which zinc phosphate coatings are used to rinse with metal with the aid of zinc phosphate detachments following the phosphating zone, the rinsing water is fed to the phosphating zone and so much water evaporates that the rinsing water is absorbed can be.
  • a content of nitrite is provided in the phosphating solution, which is adjusted by adding alkali and / or ammonium nitrite.
  • a steady state with regard to the ions contained in the phosphating solution cannot be achieved without occasional or at least partial draining.
  • DE-B-1031083 describes a process for the regeneration of zinc phosphate solutions containing nitrite and nitrate, in which, in addition to the addition of zinc, phosphate and nitrate, nitrite, preferably sodium nitrite, is also added. In this case, too, the occasional draining of the phosphating solution mentioned above cannot be avoided.
  • the object of the invention is to provide a process for producing phosphate coatings on metals, in particular steel, galvanized steel, alloy-galvanized steel, aluminized steel and aluminum, with the aid of zinc phosphate solutions containing iron (II) and nitrate ions, which works free of waste water and the known ones , especially the aforementioned, does not have disadvantages.
  • wastewater-free in the sense of the invention means that no water from the rinsing baths enters the sewage system or the receiving water with the intended effect of counteracting an accumulation of undesirable chemicals in the phosphating bath.
  • the method according to the invention is particularly suitable for the surface treatment of iron and steel, low-alloy steel, galvanized steel, alloy-galvanized, i.e. e.g. steel coated with ZnAl, ZnFe and ZnNi, aluminized steel, aluminum and its alloys.
  • the phosphating solutions contain Zn, P2O5 and NO3 as basic components. Other cations and / or anions can also be present. Phosphating solutions in which certain concentrations of bromate, chlorate, organic nitro compounds, perborate and / or persulfate have to be maintained during the work by supplementing them are not suitable for the wastewater-free procedure according to the invention. Likewise unsuitable are those to which alkali nitrite must be added as an accelerator from time to time or continuously.
  • the metal surfaces should be brought into contact with a phosphating solution in which the weight ratio (Mg + Ca + Mn + Ni + Co): Zn equal / less than 4: 1 and that of the components Mg, Ca, Mn, Fe, Ni, Co and Cu according to the molar ratio (Mg + Ca + Mn + Fe + Ni + Co + Cu): Zn equal to / less than 2 is added.
  • a phosphating solution in which the weight ratio (Mg + Ca + Mn + Ni + Co): Zn equal / less than 4: 1 and that of the components Mg, Ca, Mn, Fe, Ni, Co and Cu according to the molar ratio (Mg + Ca + Mn + Fe + Ni + Co + Cu): Zn equal to / less than 2 is added.
  • Fe (II) is usually not added as a chemical, but it accumulates during the throughput of iron and steel as a result of the pickling attack, provided that it has not been converted into the trivalent form by oxidizing agents and as iron ( III) -phosphate is precipitated.
  • Fe (III) in the baths serves, among other things, to stabilize the phosphating balance.
  • Mg and / or Ca and / or Mn phosphate coatings are obtained which, in addition to Zn and optionally Fe (II), also contain these cations.
  • Mixed phosphates of this type are notable for increased alkali resistance and are therefore particularly suitable as a primer for paints. But they have also proven themselves as a lubricant carrier in non-cutting cold forming.
  • Ni and / or Co are preferably used to reduce the aggressiveness of the baths Increase steel and improve the phosphating of zinc surfaces. Small amounts of copper have an accelerating effect.
  • Alkaline cations and / or ammonium serve primarily to set the desired acid ratio.
  • the anions F, BF4 and SiF6 generally increase the rate of phosphating and are advantageous for the treatment of aluminum-containing zinc surfaces.
  • the presence of free fluoride (F ⁇ ) is essential for the crystalline phosphating of aluminum and its alloys.
  • Cl can be used to adjust the electronic neutrality of the baths and in special cases also to increase their aggressiveness.
  • the thickness or weight per unit area of the phosphate layers produced can be influenced by adding, for example, polyhydroxyarboxylic acid, such as tartaric acid and / or citric acid.
  • the coordination of the type and amount of anions and cations in the phosphating solutions used to carry out the process according to the invention is carried out in such a way that the ratio of free P2O5 to total P2O5 (0.04 to 0.50): 1, with higher (lower ) Bath temperatures and / or concentrations in the phosphating solution each have to be chosen to be higher (lower) ratios.
  • the concentration of Fe (II) should be at most that of zinc, while the sum of the concentrations of Mg + Ca + Mn + Ni + Co should not exceed four times the zinc concentration.
  • the molar ratio of (Mg + Ca + Mn + Fe + Ni + Co + Cu): Zn should be 2: 1.
  • the supplement is particularly effective if, according to a further preferred embodiment of the invention, the metal surfaces are brought into contact with a phosphating solution, which by adding phosphate with a ratio of free P2O5 to total P2O5 when supplementing (- 0.4 to + 0.5): 1 is added.
  • a phosphating solution which by adding phosphate with a ratio of free P2O5 to total P2O5 when supplementing (- 0.4 to + 0.5): 1 is added.
  • the minus sign means that there is no free P2O5, but rather part of the phosphate is in the secondary phosphate stage.
  • the value minus 0.19 means, for example, that 19% of the total P2O5 are present as secondary phosphate.
  • the phosphate components in the supplement are in a range which is 40% secondary and 60% primary phosphate (calc. As P2O5 on the one hand and 50% primary phosphate and 50% free phosphoric acid (calc. As P2O5) on the other hand is limited.
  • the supplementary components are usually added in the form of an acidic aqueous chemical concentrate. Since liquid supplement concentrates with a ratio of free P2O5 to total P2O5 less than 0.2: 1 are not stable, the supplement is then carried out with at least two separate concentrates.
  • the rate of addition is expediently chosen such that the composition of the phosphating solution is at least largely constant even with fluctuating throughput, ie fluctuating consumption remains.
  • Special portions of the necessary supplement can also be added to the bath separately from the actual supplement concentrate.
  • An example is the addition of zinc oxide or zinc carbonate, which on the one hand increases the zinc concentration and on the other hand a correction of the ratio of free P2O5 to total P2O5 is possible.
  • NO3 optionally together with oxygen-containing gas, H2O2 and / or nitrous gases are used as oxidation accelerators in the process according to the invention.
  • a small amount of nitrite, about 0.05 to 0.15 g / l, for example as zinc nitrite or calcium nitrite is preferably added at the start of work.
  • the nitrite generation from the nitrate can also be initiated by brief phosphating of zinc, zinc granules or zinc dust or by initially lower throughput density of steel.
  • Alkali nitrite should only be used in exceptional cases when starting the bath, otherwise alkali will accumulate to a disruptive extent. Due to the absence of excess nitrite or H2O5 accumulates in the baths (Fe (II) when iron and steel are treated. Intensive contact of the solution with oxygen-containing gas, such as air, and / or H2O2 can enrich the iron via the Interference limit can be avoided.
  • oxygen-containing gas such as air
  • the rinsing step is followed by a rinsing bath cascade with at least two rinsing baths.
  • the principle of the rinsing bath cascade is that fresh water is only supplied to the last rinsing bath and a corresponding overflow into the preceding baths is triggered. In this way, a rinse water flow manufactured, which is opposite to the flow of the workpieces.
  • the fluid transfer to the workpieces, the number of rinsing baths in the cascade and the concentration of the phosphating solution, there are different impurity concentrations in the individual rinsing baths see Table 1).
  • At least as much low-salt or salt-free water is withdrawn from the phosphating bath by a suitable process that it can absorb the phosphate-rich overflow from the cascade.
  • the characteristics of the cascade should be selected so that the degree of purity of the last rinsing bath is sufficient for the technical requirements of the further treatments.
  • the effectiveness of a rinsing bath cascade can be increased even more by not overflowing directly from one bath into the previous one, but in such a way that the parts running out of the previous bath are sprayed off first and only then is it introduced into the rinsing bath itself.
  • Further preferred embodiments of the method according to the invention consist in extracting the salt-free or low-salt water from the phosphating bath by means of single-stage or multi-stage evaporation, reverse osmosis or electrodialysis and returning it to the rinsing bath cascade as fresh water.
  • a further preferred embodiment provides for the phosphate-containing rinsing water from the rinsing bath cascade to be concentrated, in particular by evaporation, electrodialysis or reverse osmosis, before they are introduced into the phosphating bath.
  • a bath sludge is obtained, which is separated from the system continuously or from time to time, for example by sedimentation, filtration and the like. 50 to 90% of the phosphating solution adheres to this wet sludge.
  • this phosphate sludge is washed with water after it has been separated off and introduced into the rinsing bath cascade or directly into the phosphating bath.
  • the phosphate sludge can be washed in several stages, possibly in the manner of a cascade, with rinsing water from the individual rinsing baths.
  • a 3-stage rinse bath cascade followed the phosphating. During the material throughput, 0.2 l / m2 of treated steel surface were evaporated from the phosphating bath. In the last rinsing bath of the cascade, 0.2 l of salt-free water per m2 of treated surface were added. The resulting overflow reached rinsing bath 2, rinsing bath 1 and finally the phosphating bath.
  • Table 2 lists various phosphating bath compositions suitable for carrying out the process according to the invention and supplementary concentrates suitable therefor.

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  • 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)
  • Materials For Medical Uses (AREA)
EP90202148A 1989-08-22 1990-08-07 Verfahren zur Erzeugung von Phosphatüberzügen auf Metalloberflächen Expired - Lifetime EP0414301B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT90202148T ATE85987T1 (de) 1989-08-22 1990-08-07 Verfahren zur erzeugung von phosphatueberzuegen auf metalloberflaechen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3927613 1989-08-22
DE3927613A DE3927613A1 (de) 1989-08-22 1989-08-22 Verfahren zur erzeugung von phosphatueberzuegen auf metalloberflaechen

Publications (2)

Publication Number Publication Date
EP0414301A1 EP0414301A1 (de) 1991-02-27
EP0414301B1 true EP0414301B1 (de) 1993-02-24

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ID=6387565

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90202148A Expired - Lifetime EP0414301B1 (de) 1989-08-22 1990-08-07 Verfahren zur Erzeugung von Phosphatüberzügen auf Metalloberflächen

Country Status (12)

Country Link
US (1) US5203930A (ja)
EP (1) EP0414301B1 (ja)
JP (1) JP3000108B2 (ja)
AT (1) ATE85987T1 (ja)
AU (1) AU633611B2 (ja)
BR (1) BR9004128A (ja)
CA (1) CA2023663C (ja)
DD (1) DD299661A5 (ja)
DE (2) DE3927613A1 (ja)
ES (1) ES2038483T3 (ja)
PL (1) PL164655B1 (ja)
ZA (1) ZA906672B (ja)

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JP3479609B2 (ja) 1999-03-02 2003-12-15 日本パーカライジング株式会社 スラッジ発生のないリン酸亜鉛処理液およびリン酸亜鉛処理方法
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JP4658339B2 (ja) * 2001-01-17 2011-03-23 日本ペイント株式会社 金属表面処理方法
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US8062435B2 (en) * 2001-06-18 2011-11-22 Henkel Kommanditgesellschaft Auf Aktien Phosphating operation
JP4544970B2 (ja) * 2004-11-09 2010-09-15 Jfeスチール株式会社 酸洗廃液の処理方法および酸洗廃液用処理装置
JP2007190322A (ja) * 2006-01-23 2007-08-02 Aisin Seiki Co Ltd ベッド装置
KR102070497B1 (ko) * 2018-02-01 2020-01-28 한양대학교 에리카산학협력단 나노 결정체를 포함하는 금속 구조물, 및 그 제조 방법

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JPH0387375A (ja) 1991-04-12
BR9004128A (pt) 1991-09-03
AU6118590A (en) 1991-02-28
DE3927613A1 (de) 1991-02-28
US5203930A (en) 1993-04-20
DD299661A5 (de) 1992-04-30
ES2038483T3 (es) 1993-07-16
ZA906672B (en) 1992-04-29
ATE85987T1 (de) 1993-03-15
CA2023663C (en) 1998-11-03
EP0414301A1 (de) 1991-02-27
JP3000108B2 (ja) 2000-01-17
DE59000923D1 (de) 1993-04-01
PL164655B1 (pl) 1994-08-31
PL286573A1 (en) 1991-07-15
CA2023663A1 (en) 1991-02-23
AU633611B2 (en) 1993-02-04

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