EP0324395A1 - Process for phosphatizing metal surfaces - Google Patents
Process for phosphatizing metal surfaces Download PDFInfo
- Publication number
- EP0324395A1 EP0324395A1 EP89100228A EP89100228A EP0324395A1 EP 0324395 A1 EP0324395 A1 EP 0324395A1 EP 89100228 A EP89100228 A EP 89100228A EP 89100228 A EP89100228 A EP 89100228A EP 0324395 A1 EP0324395 A1 EP 0324395A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- ions
- metal surfaces
- zinc
- phosphating
- contact
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 28
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 22
- 239000002184 metal Substances 0.000 title claims abstract description 22
- 230000008569 process Effects 0.000 title claims abstract description 21
- 239000000243 solution Substances 0.000 claims abstract description 31
- -1 Ca2+ ions Chemical class 0.000 claims abstract description 18
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000011701 zinc Substances 0.000 claims abstract description 14
- 239000002253 acid Substances 0.000 claims abstract description 13
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 12
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 9
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 9
- 229910052742 iron Inorganic materials 0.000 claims abstract description 9
- 229910001424 calcium ion Inorganic materials 0.000 claims abstract description 8
- 239000000956 alloy Substances 0.000 claims abstract description 7
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 7
- 150000002828 nitro derivatives Chemical class 0.000 claims abstract description 7
- 230000004913 activation Effects 0.000 claims abstract description 3
- 239000007864 aqueous solution Substances 0.000 claims abstract description 3
- 229910000831 Steel Inorganic materials 0.000 claims description 11
- 239000010959 steel Substances 0.000 claims description 11
- 229910019142 PO4 Inorganic materials 0.000 claims description 8
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 6
- 239000010452 phosphate Substances 0.000 claims description 5
- IDCPFAYURAQKDZ-UHFFFAOYSA-N 1-nitroguanidine Chemical compound NC(=N)N[N+]([O-])=O IDCPFAYURAQKDZ-UHFFFAOYSA-N 0.000 claims description 2
- ONMOULMPIIOVTQ-UHFFFAOYSA-N 98-47-5 Chemical class OS(=O)(=O)C1=CC=CC([N+]([O-])=O)=C1 ONMOULMPIIOVTQ-UHFFFAOYSA-N 0.000 claims description 2
- 238000007598 dipping method Methods 0.000 claims description 2
- 150000002222 fluorine compounds Chemical class 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- 238000005482 strain hardening Methods 0.000 abstract description 2
- 230000001747 exhibiting effect Effects 0.000 abstract 1
- 239000000344 soap Substances 0.000 description 14
- IQBJFLXHQFMQRP-UHFFFAOYSA-K calcium;zinc;phosphate Chemical compound [Ca+2].[Zn+2].[O-]P([O-])([O-])=O IQBJFLXHQFMQRP-UHFFFAOYSA-K 0.000 description 6
- 235000021317 phosphate Nutrition 0.000 description 6
- 230000008901 benefit Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000003513 alkali Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000007654 immersion Methods 0.000 description 4
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 3
- QNNXEUPKHFCUKS-UHFFFAOYSA-J [Ca+2].[Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O Chemical compound [Ca+2].[Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O QNNXEUPKHFCUKS-UHFFFAOYSA-J 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 229910000398 iron phosphate Inorganic materials 0.000 description 3
- WBJZTOZJJYAKHQ-UHFFFAOYSA-K iron(3+) phosphate Chemical compound [Fe+3].[O-]P([O-])([O-])=O WBJZTOZJJYAKHQ-UHFFFAOYSA-K 0.000 description 3
- RYYKJJJTJZKILX-UHFFFAOYSA-M sodium octadecanoate Chemical compound [Na+].CCCCCCCCCCCCCCCCCC([O-])=O RYYKJJJTJZKILX-UHFFFAOYSA-M 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- IHBCFWWEZXPPLG-UHFFFAOYSA-N [Ca].[Zn] Chemical compound [Ca].[Zn] IHBCFWWEZXPPLG-UHFFFAOYSA-N 0.000 description 2
- 239000010953 base metal Substances 0.000 description 2
- 229960005069 calcium Drugs 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical class [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000014593 oils and fats Nutrition 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 2
- 238000005554 pickling Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 2
- LRXTYHSAJDENHV-UHFFFAOYSA-H zinc phosphate Chemical compound [Zn+2].[Zn+2].[Zn+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O LRXTYHSAJDENHV-UHFFFAOYSA-H 0.000 description 2
- 229910000165 zinc phosphate Inorganic materials 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- VTLYFUHAOXGGBS-UHFFFAOYSA-N Fe3+ Chemical compound [Fe+3] VTLYFUHAOXGGBS-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000006887 Ullmann reaction Methods 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000001642 boronic acid derivatives Chemical class 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 238000011086 high cleaning Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical class [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 description 1
- 235000019359 magnesium stearate Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 229940085991 phosphate ion Drugs 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- 238000004506 ultrasonic cleaning Methods 0.000 description 1
- 238000005491 wire drawing Methods 0.000 description 1
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 1
- LKCUKVWRIAZXDU-UHFFFAOYSA-L zinc;hydron;phosphate Chemical compound [Zn+2].OP([O-])([O-])=O LKCUKVWRIAZXDU-UHFFFAOYSA-L 0.000 description 1
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
- 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
- C23C22/05—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 using aqueous solutions
- C23C22/06—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 using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/07—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing phosphates
- C23C22/08—Orthophosphates
- C23C22/22—Orthophosphates containing alkaline earth metal cations
-
- 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
- C23C22/05—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 using aqueous solutions
- C23C22/06—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 using aqueous solutions using aqueous acidic solutions with pH less than 6
- C23C22/34—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
- C23C22/36—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates
- C23C22/367—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 using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also phosphates containing alkaline earth metal cations
Definitions
- the present invention relates to a method for phosphating metal surfaces, in particular the zinc-calcium phosphating of surfaces made of iron, steel, zinc and / or aluminum as a pretreatment for cold forming.
- Zinc phosphating baths can contain, for example, monozinc phosphate, free phosphoric acid, zinc nitrate and oxidizing agents as main components.
- the pH of such solutions is usually in the range between 2.8 and 3.4.
- the process sequence consists of two reactions, the pickling reaction and the formation of a zinc phosphate layer on the surface to be phosphated.
- the alkali phosphating processes clean and degrease the metal surface and form a corrosion-protective cover layer, which mainly consists of iron phosphate.
- the layer formation is initiated by a pickling reaction in which a small amount of the base metal is removed.
- the majority of the dissolved surface material reacts with the phosphate ion of the solution to form poorly soluble phosphates, which deposit as a firmly adhering coating on the surface.
- the layer-forming cation originates from the base metal itself.
- iron phosphate layers with a low layer weight of around 0.2 to 0.4 g / m2 and iron phosphate layers with higher basis weights from 0.6 to 1.2 g / m2.
- the thin phosphate layers are particularly suitable for painting; they ensure excellent paint adhesion, offer good rust protection, electrical insulation, reduction of sliding resistance and facilitate cold forming.
- phosphate layers with a layer weight of up to 40 g / m2 are usually deposited.
- the metal soaps are known to be produced.
- Aluminum, calcium, lithium, zinc and magnesium stearates are water-repellent and, as solid lubricants in wire drawing, result in lower coefficients of friction at higher surface pressures than conventional alkali soaps.
- Metal soaps have the advantage over alkali soaps that they hardly absorb moisture from the air, remain unchanged in their lubricating effect due to their high compressive strength and allow higher overall cross-sectional decreases, while with alkaline soaps the lubricating effect can decrease significantly due to moisture absorption.
- EP-PS 0 045 110 describes a process for the production of phosphate coatings on iron or steel surfaces by immersion or flooding with an aqueous acidic zinc phosphate solution, the surfaces being brought into contact with a solution which, in addition to Zn2+, PO43 ⁇ , NO3 ⁇ or contains an equivalent iron (II) non-oxidizing accelerator in which the weight ratio Zn: PO4 is greater than 0.8, the ratio of total acid to free acid is at least 5 and in which one by suitable measurement of ClO3 ⁇ or an equivalent Iron (II) to iron (III) oxidizing accelerator sets an iron (II) content of 0.05 to 1 wt .-%.
- the object of the present invention was to provide an improved method for phosphating metal surfaces, in particular surfaces made of iron, steel, zinc and their alloys, as well as aluminum as a pretreatment for cold forming.
- the objects of the present invention are achieved by the improved phosphating process based on zinc-calcium-phosphate layers.
- the phosphating solution with which the surfaces to be coated are brought into contact can Zn2+ and Ca2+ ions in a weight ratio of 1: 0.5 to 1: 1.5 and preferably in a ratio of 1: 1.
- preferred embodiments of the present phosphating solution contain further cations of transition metal ions in addition to the above Ca2 und and Zn2+ cations.
- Ni2+ ions are particularly preferred at this point.
- the phosphating solutions contain Ni2+ ions, an amount of 0.01 to 10 g / l of Ni2+ ions is preferred.
- phosphating solutions according to the invention can contain further additional anions.
- simple and / or complex fluorides can be used as further anions, if appropriate. These can be used in the phosphating solutions in particular in amounts of 0.01 to 10 g / l.
- a preferred embodiment of the present invention is to set the temperature range in the range from 50 to 70 ° C. and to bring the metal surfaces into contact with the phosphating solutions.
- phosphating solutions according to the invention can contain 0.1 to 2.0 g of organic nitro compounds.
- Organic nitro compounds in the sense of the present invention are selected from m-nitrobenzenesulfonates and / or nitroguanidine.
- the organic nitro compounds can also be present in amounts of 0.1 to 2.0 g / l in addition to 10 to 100 g / l NO3 ⁇ ions in the phosphating solutions.
- the process for phosphating metal surfaces in particular surfaces made of iron, steel, zinc and their alloys, as well as aluminum, zinc-calcium-phosphate layers (Scholzit) with a basis weight of 3 to 9 g / m2 are produced.
- Scholzit zinc-calcium-phosphate layers
- the zinc-calcium-phosphate layers can be created on the metal surfaces by dipping, spraying and flooding as well as by combined processes.
- the surfaces to be phosphated are degreased according to the methods known in the prior art.
- Oil, grease and lubricant residues or grinding dust from previous manufacturing processes can be removed by organic solvents or aqueous cleaners.
- the chlorinated hydrocarbons are the most frequently used organic solvents because they dissolve oils and fats excellently and are not flammable. Solids and inorganic contaminants, however, are only removed inadequate. Water-based cleaners have a very high cleaning ability.
- the advantage of the present invention is that zinc-calcium-phosphate layers are suitable for producing low layer weights on the order of 3 to 9 g / m 2 on wire.
- the zinc-calcium-phosphate layers largely contain the mineral scholzite.
- a mixed soap of zinc-calcium stearate is formed in addition to zinc stearate and calcium stearate.
- zinc calcium stearate has the advantage that the durability of the drawing dies is increased many times over. Pulling tests in the technical center also showed that the wire surfaces, in particular during a subsequent polishing pull, achieve a substantially brighter and more uniform appearance than can be achieved with conventional methods operated on the accelerator side.
- Another product advantage is the fact that the new zinc-calcium phosphating process for cold working works in a temperature range of preferably 50 to 70 ° C.
- the sludge behavior in this process can be classified as particularly favorable, since even after a bath load of 1.5 m2 steel surface per liter of bath solution, only minimal quantities in the order of a few milliliters of bath sludge are produced.
- Another advantage of the present invention is that the Sales with drawing soap (sodium stearate) resulting zinc-calcium stearate mixed soaps allow a longer service life of the drawing dies due to the improved properties.
- a phosphating solution was prepared that 10.3 gl ⁇ 1 Ca2+ ions 14.0 gl ⁇ 1 Zn2+ ions 27.8 gl ⁇ 1 PO43 ⁇ ions 46.5 gl ⁇ 1 NO3 ⁇ ions contained.
- the phosphating solution had the following characteristics: pH: approx.2.6 Acid ratio: approx. 1:21 (free acid to total acid)
- the pH was 2.5 and the ratio of free Acid to total acid 1: 17.6.
- the wire coated in this way could easily be reduced to the desired size using several drawing dies connected in series.
- the result was a bright and shiny surface.
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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)
- Laminated Bodies (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
Die vorliegende Erfindung betrifft ein Verfahren zur Phosphatierung von Metalloberflächen, insbesondere die Zink-Calcium-Phosphatierung von Oberflächen aus Eisen, Stahl, Zink und/oder Aluminium als Vorbehandlung für die Kaltumformung.The present invention relates to a method for phosphating metal surfaces, in particular the zinc-calcium phosphating of surfaces made of iron, steel, zinc and / or aluminum as a pretreatment for cold forming.
Verfahren zum Phosphatieren von Oberflächen aus Eisen, Stahl, Zink und deren Legierungen sowie Aluminium sind seit langem bekannt (Ullmanns Encyklopädie der technischen Chemie, 4. Auflage, Band 15 Seite 686 f). Das Phosphatieren der genannten Oberflächen dient zur Erhöhung der Haftfestigkeit von Lackschichten und zur Verbesserung des Korrosionsschutzes.Processes for phosphating surfaces made of iron, steel, zinc and their alloys as well as aluminum have long been known (Ullmanns Encyklopadie der Technische Chemie, 4th edition, volume 15 page 686 f). The phosphating of the surfaces mentioned serves to increase the adhesive strength of paint layers and to improve corrosion protection.
Die größte Bedeutung der Phosphatierverfahren besitzen das Zink- und das Alkaliphosphatieren. Zinkphosphatierbäder können beispielsweise Monozinkphosphat, freie Phosphorsäure, Zinknitrat und Oxidationsmittel als Hauptkomponenten enthalten. Der pH-Wert solcher Lösungen liegt üblicherweise im Bereich zwischen 2,8 und 3,4. Der Verfahrensablauf besteht aus zwei Reaktionen, der Beizreaktion und der Bildung einer Zinkphosphatschicht auf der zu phosphatierenden Oberfläche.The most important of the phosphating processes are zinc and alkali phosphating. Zinc phosphating baths can contain, for example, monozinc phosphate, free phosphoric acid, zinc nitrate and oxidizing agents as main components. The pH of such solutions is usually in the range between 2.8 and 3.4. The process sequence consists of two reactions, the pickling reaction and the formation of a zinc phosphate layer on the surface to be phosphated.
Im Gegensatz dazu reinigen und entfetten die Alkaliphosphatierverfahren die Metalloberfläche und bilden eine korrosionsschützende Deckschicht aus, die hauptsächlich aus Eisenphosphat besteht. Die Schichtbildung wird durch eine Beizreaktion eingeleitet, bei der eine geringe Menge des Grundmetalls abgelöst wird. Der überwiegende Teil des gelösten Oberflächenmaterials reagiert mit dem Phosphation der Lösung unter Bildung von schwerlöslichen Phosphaten, die sich als festhaftender Überzug auf der Oberfläche abscheiden. Im Gegensatz zur Zinkphosphatierung stammt hier das schichtbildende Kation aus dem Grundmetall selbst.In contrast, the alkali phosphating processes clean and degrease the metal surface and form a corrosion-protective cover layer, which mainly consists of iron phosphate. The layer formation is initiated by a pickling reaction in which a small amount of the base metal is removed. The majority of the dissolved surface material reacts with the phosphate ion of the solution to form poorly soluble phosphates, which deposit as a firmly adhering coating on the surface. In contrast to zinc phosphating, the layer-forming cation originates from the base metal itself.
Prinzipiell kann bei der Korrosionsschutzphosphatierung zwischen zwei Schichttypen unterschieden werden: Eisenphosphatschichten mit niedrigem Schichtgewicht von etwa 0,2 bis 0,4 g/m² und Eisenphosphatschichten mit höheren Flächengewichten von 0,6 bis 1,2 g/m². Für eine Lackierung sind die dünnen Phosphatschichten besonders geeignet; sie gewähren eine vorzügliche Lackhaftung, bieten einen guten Unterrostungsschutz, elektrische Isolation, Verminderung des Gleitwiderstandes und erleichtern die Kaltumformung.In principle, a distinction can be made between corrosion protection phosphating between two types of layers: iron phosphate layers with a low layer weight of around 0.2 to 0.4 g / m² and iron phosphate layers with higher basis weights from 0.6 to 1.2 g / m². The thin phosphate layers are particularly suitable for painting; they ensure excellent paint adhesion, offer good rust protection, electrical insulation, reduction of sliding resistance and facilitate cold forming.
Für die Kaltumformung werden üblicherweise Phosphatschichten mit einem Schichtgewicht bis zu 40 g/m² abgeschieden. Bei Umsetzung der bekannten Phosphatschichten für die Kaltumformung mit entsprechenden Natriumstearatseifen entstehen bekanntermaßen die Metallseifen. Aluminium-, Calcium-, Lithium-, Zink- und Magnesiumstearate sind wasserabweisend und ergeben als Festschmierstoffe im Drahtzug bei höheren Flächenpressungen geringere Reibwerte als übliche Alkaliseifen.For cold forming, phosphate layers with a layer weight of up to 40 g / m² are usually deposited. When the known phosphate layers for cold forming are implemented with corresponding sodium stearate soaps, the metal soaps are known to be produced. Aluminum, calcium, lithium, zinc and magnesium stearates are water-repellent and, as solid lubricants in wire drawing, result in lower coefficients of friction at higher surface pressures than conventional alkali soaps.
Da die Schmelzpunkte niedriger sind als bei Natriumseifen und die Metallstearate für sich alleine zu fett sind, werden in der Praxis Trägerstoffe, wie beispielsweise Kalk, eingearbeitet, um die Metallseifen im Schmierspalt zu halten. Metallseifen haben gegenüber Alkaliseifen den Vorteil, daß sie kaum Feuchtigkeit aus der Luft aufnehmen, infolge ihrer hohen Druckfestigkeit in ihrer Schmierwirkung unverändert bleiben und höhere Gesamtquerschnittsabnahmen ermöglichen, während bei Alkaliseifen die Schmierwirkung durch Feuchtigkeitsaufnahme stark sinken kann.Since the melting points are lower than with sodium soaps and the metal stearates are too fat by themselves, in practice carriers such as lime are incorporated in order to keep the metal soaps in the lubrication gap. Metal soaps have the advantage over alkali soaps that they hardly absorb moisture from the air, remain unchanged in their lubricating effect due to their high compressive strength and allow higher overall cross-sectional decreases, while with alkaline soaps the lubricating effect can decrease significantly due to moisture absorption.
Die EP-PS 0 045 110 beschreibt ein Verfahren zur Herstellung von Phosphatüberzügen auf Eisen oder Stahloberflächen im Tauchverfahren oder Flutverfahren mit einer wäßrigen sauren Zinkphosphatlösung, wobei man die Oberflächen mit einer Lösung in Berührung bringt, die neben Zn²⁺, PO₄³⁻, NO₃⁻ oder eines gleich wirkenden Eisen (II) nicht oxidierenden Beschleunigers enthält, in der das Gewichtsverhältnis Zn : PO₄ größer als 0,8 ist, das Verhältnis von Gesamtsäure zu freier Säure mindestens 5 beträgt und in der man durch geeignete Bemessung von ClO₃⁻ oder einem gleich wirkenden Eisen (II) zu Eisen (III) oxidierenden Beschleuniger einen Eisen (II) gehalt von 0,05 bis 1 Gew.-% einstellt.EP-PS 0 045 110 describes a process for the production of phosphate coatings on iron or steel surfaces by immersion or flooding with an aqueous acidic zinc phosphate solution, the surfaces being brought into contact with a solution which, in addition to Zn²⁺, PO₄³⁻, NO₃⁻ or contains an equivalent iron (II) non-oxidizing accelerator in which the weight ratio Zn: PO₄ is greater than 0.8, the ratio of total acid to free acid is at least 5 and in which one by suitable measurement of ClO₃⁻ or an equivalent Iron (II) to iron (III) oxidizing accelerator sets an iron (II) content of 0.05 to 1 wt .-%.
Der vorliegenden Erfindung lag die Aufgabe zugrunde, ein verbessertes Verfahren zur Phosphatierung von Metalloberflächen, insbesondere von Oberflächen aus Eisen, Stahl, Zink und deren Legierungen sowie Aluminium als Vorbehandlung für die Kaltumformung zur Verfügung zu stellen.The object of the present invention was to provide an improved method for phosphating metal surfaces, in particular surfaces made of iron, steel, zinc and their alloys, as well as aluminum as a pretreatment for cold forming.
Die Aufgaben der vorliegenden Erfindung werden durch das verbesserte Phosphatierungsverfahren auf der Basis von Zink-Calcium-Phosphatschichten gelöst.The objects of the present invention are achieved by the improved phosphating process based on zinc-calcium-phosphate layers.
Gegenstand der vorliegenden Erfindung ist ein Verfahren zur Phosphatierung von Metalloberflächen, insbesondere von Oberflächen aus Eisen, Stahl, Zink und deren Legierungen sowie Aluminium als Vorbehandlung für die Kaltumformung, wobei man die Oberfläche in an sich bekannter Weise reinigt und/oder beizt, dadurch gekennzeichnet, daß man die Oberflächen ohne vorherige Aktivierung im Temperaturbereich von 30 bis 70 °C mit einer wäßrigen Lösung in Kontakt bringt, die
- (a) 10 bis 40 g/l Ca²⁺-Ionen,
- (b) 10 bis 40 g/l Zn²⁺-Ionen,
- )c) 10 bis 100 g/l PO₄³⁻-Ionen
- (d) 10 bis 100 g/l NO₃⁻-Ionen und/oder
- (e) 0,1 bis 2,0 g/l organische Nitroverbindungen,
wobei die Lösung einen pH-Wert im Bereich von 2,0 bis 3,8 und ein Verhältnis von feier Säure zu Gesamtsäure von 1 : 4 bis 1 : 100 aufweist.The present invention relates to a process for phosphating metal surfaces, in particular surfaces made of iron, steel, zinc and their alloys and aluminum as pretreatment for cold forming, the surface being cleaned and / or pickled in a manner known per se, characterized in that that the surfaces are brought into contact with an aqueous solution in the temperature range from 30 to 70 ° C. without prior activation
- (a) 10 to 40 g / l Ca²⁺ ions,
- (b) 10 to 40 g / l Zn²⁺ ions,
- ) c) 10 to 100 g / l PO₄³⁻ ions
- (d) 10 to 100 g / l NO₃⁻ ions and / or
- (e) 0.1 to 2.0 g / l organic nitro compounds,
the solution having a pH in the range of 2.0 to 3.8 and a ratio of acid to total acid of 1: 4 to 1: 100.
Überraschenderweise wurde trotz des gegenüber der EP-PS 0 045 101 verschiedenen Zn : Ca Verhältnisses und den hohen Calcium-Anteilen die nach dem Stand der Technik nicht zu erwartende Schichtausbildung bei der hohen Konzentration des Ca-Ions in der Phosphatierungslösung gefunden.Surprisingly, in spite of the different Zn: Ca ratio compared to EP-PS 0 045 101 and the high calcium proportions, the layer formation not to be expected according to the prior art was found at the high concentration of the Ca ion in the phosphating solution.
Gemäß einer bevorzugten Ausführungsform der vorliegenden Erfindung kann die Phosphatierlösung, mit der man die zu beschichtenden Oberflächen in Kontakt bringt, Zn²⁺- und Ca²⁺-Ionen im Gewichtsverhältnis von 1 : 0,5 bis 1 : 1,5 und vorzugsweise im Verhältnis von 1 : 1 enthalten.According to a preferred embodiment of the present invention, the phosphating solution with which the surfaces to be coated are brought into contact can Zn²⁺ and Ca²⁺ ions in a weight ratio of 1: 0.5 to 1: 1.5 and preferably in a ratio of 1: 1.
Vorteilhafterweise enthalten bevorzugte Ausführungsformen der vorliegenden Phosphatierlösung zusätzlich zu den oben genannten Ca²⁺- und Zn²⁺-Kationen weitere Kationen von Übergangsmetallionen. Insbesondere bevorzugt sind an dieser Stelle Ni²⁺-Ionen. In dem Falle, daß die Phosphatierlösungen Ni²⁺-Ionen enthalten, ist eine Menge von 0,01 bis 10 g/l an Ni²⁺-Ionen bevorzugt.Advantageously, preferred embodiments of the present phosphating solution contain further cations of transition metal ions in addition to the above Ca² und and Zn²⁺ cations. Ni²⁺ ions are particularly preferred at this point. In the case that the phosphating solutions contain Ni²⁺ ions, an amount of 0.01 to 10 g / l of Ni²⁺ ions is preferred.
Zusätzlich zu den genannten Anionen wie PO₄³⁻- und NO₃⁻-Ionen können erfindungsgemäße Phosphatierlösungen weitere zusätzliche Anionen enthalten. Als gegebenenfalls zu verwendende weitere Anionen kommen gemäß einer bevorzugten Ausführungsform einfache und/oder komplexe Fluoride in Frage. Diese können in den Phosphatierlösungen insbesondere in Mengen von 0,01 bis 10 g/l verwendet werden.In addition to the anions mentioned, such as PO₄³⁻ and NO₃⁻ ions, phosphating solutions according to the invention can contain further additional anions. According to a preferred embodiment, simple and / or complex fluorides can be used as further anions, if appropriate. These can be used in the phosphating solutions in particular in amounts of 0.01 to 10 g / l.
Während üblicherweise das erfindungsgemäße Phosphatierungsverfahren im Bereich von 30 bis 70 °C durchgeführt wird, besteht eine bevorzugte Ausführungsform der vorliegenden Erfindung darin, den Temperaturbereich im Bereich von 50 bis 70 °C einzustellen und die Metalloberflächen mit den Phosphatierlösungen in Kontakt zu bringen.While the phosphating process according to the invention is usually carried out in the range from 30 to 70 ° C., a preferred embodiment of the present invention is to set the temperature range in the range from 50 to 70 ° C. and to bring the metal surfaces into contact with the phosphating solutions.
Anstelle von 10 bis 100 g/l NO₃⁻-Ionen können erfindungsgemäße Phosphatierungslösungen 0,1 bis 2,0 g organische Nitroverbindungen enthalten. Organische Nitroverbindungen im Sinne der vorliegenden Erfindung sind ausgewählt aus m-Nitrobenzolsulfonaten und/oder Nitroguanidin. Die organischen Nitroverbindungen können auch in Mengen von 0,1 bis 2,0 g/l neben 10 bis 100 g/l NO₃⁻-Ionen in den Phosphatierungslösungen vorliegen. Gemäß einer Ausführungsform der vorliegenden Erfindung werden durch das Verfahren zur Phosphatierung von Metalloberflächen, insbesondere von Oberflächen aus Eisen, Stahl, Zink und deren Legierungen sowie Aluminium, Zink-Calcium-Phosphatschichten (Scholzit) mit einem Flächengewicht von 3 bis 9 g/m² erzeugt.Instead of 10 to 100 g / l of NO₃⁻ ions, phosphating solutions according to the invention can contain 0.1 to 2.0 g of organic nitro compounds. Organic nitro compounds in the sense of the present invention are selected from m-nitrobenzenesulfonates and / or nitroguanidine. The organic nitro compounds can also be present in amounts of 0.1 to 2.0 g / l in addition to 10 to 100 g / l NO₃⁻ ions in the phosphating solutions. According to one embodiment of the present invention, the process for phosphating metal surfaces, in particular surfaces made of iron, steel, zinc and their alloys, as well as aluminum, zinc-calcium-phosphate layers (Scholzit) with a basis weight of 3 to 9 g / m² are produced.
Die Zink-Calcium-Phosphatschichten können auf den Metalloberflächen durch Tauchen, Spritzen und Fluten sowie durch kombinierte Verfahren erzeugt werden. Vor der Anwendung des erfindungsgemäßen Verfahrens zur Phosphatierung werden die zu phosphatierenden Oberflächen nach den im Stand der Technik bekannten Verfahren entfettet. Von vorangegangenen Fertigungsprozessen stammende Öl-, Fett- und Schmierstoffreste oder Schleifstaub können durch organische Lösemittel oder wäßrige Reiniger entfernt werden. Die chlorierten Kohlenwasserstoffe sind die am häufigsten angewendeten organischen Lösungsmittel, da sie Öle und Fette ausgezeichnet lösen und nicht brennbar sind. Feststoffe und anorganische Verunreinigungen werden jedoch nur mangelhaft entfernt. Reiniger auf wäßriger Basis haben ein sehr hohes Reinigungsvermögen. Sie enthalten oberflächenaktive Substanzen, die Öle und Fette im Wasser emulgieren, sowie anorganische Bestandteile, wie Carbonate, Silikate, Borate und Phosphate, die alkalisch reagieren und natürliche Fette verseifen. Eine weitere Möglichkeit der Vorreinigung vor der Phosphatierung besteht darin, die zu phosphatierenden Metallober flächen einer Ultraschallreinigung oder einer mechanischen Reinigung zu unterziehen.The zinc-calcium-phosphate layers can be created on the metal surfaces by dipping, spraying and flooding as well as by combined processes. Before the method for phosphating according to the invention is used, the surfaces to be phosphated are degreased according to the methods known in the prior art. Oil, grease and lubricant residues or grinding dust from previous manufacturing processes can be removed by organic solvents or aqueous cleaners. The chlorinated hydrocarbons are the most frequently used organic solvents because they dissolve oils and fats excellently and are not flammable. Solids and inorganic contaminants, however, are only removed inadequate. Water-based cleaners have a very high cleaning ability. They contain surface-active substances that emulsify oils and fats in the water, as well as inorganic components such as carbonates, silicates, borates and phosphates, which have an alkaline reaction and saponify natural fats. A further possibility of pre-cleaning before phosphating is the metal surface to be phosphated surfaces to undergo ultrasonic cleaning or mechanical cleaning.
Der Vorteil der vorliegenden Erfindung besteht darin, daß Zink-Calcium-Phosphatschichten geeignet sind, auf Draht niedrige Schichtgewichte in der Größenordnung von 3 bis 9 g/m² zu erzeugen.The advantage of the present invention is that zinc-calcium-phosphate layers are suitable for producing low layer weights on the order of 3 to 9 g / m 2 on wire.
Die gebildeten Zink-Calcium-Phosphatschichten enthalten größtenteils das Mineral Scholzit. Beim Umsetzen der Zink-Calcium-Phosphatschichten mit den in der Technik verwendeten Natriumstearatseifen entsteht neben Zinkstearat und Calciumstearat auch eine Mischseife aus Zink-Calciumstearat.The zinc-calcium-phosphate layers largely contain the mineral scholzite. When the zinc-calcium-phosphate layers are reacted with the sodium stearate soaps used in the technology, a mixed soap of zinc-calcium stearate is formed in addition to zinc stearate and calcium stearate.
Zink-Calciumstearat hat ziehtechnisch den Vorteil, daß die Haltbarkeit der Ziehsteine um ein vielfaches erhöht wird. Ziehversuche im Technikum ergaben weiterhin, daß die Drahtoberflächen, insbesondere bei einem nachfolgenden Polierzug, eine wesentliche hellere und gleichmäßigere Optik erzielen, als dies bei herkömmliche, auf der Beschleunigerseite gefahrenen Verfahren erreicht werden kann.In terms of drawing technology, zinc calcium stearate has the advantage that the durability of the drawing dies is increased many times over. Pulling tests in the technical center also showed that the wire surfaces, in particular during a subsequent polishing pull, achieve a substantially brighter and more uniform appearance than can be achieved with conventional methods operated on the accelerator side.
Ein weiterer Produktvorteil ist darin zu sehen, daß das neue Zink-Calcium-Phosphatierungsverfahren für die Kaltverformung in einem Temperaturbereich von vorzugsweise 50 bis 70 °C arbeitet. Das Schlammverhalten ist bei diesem Verfahren als besonders günstig einzustufen, da selbst nach einer Badbelastung von 1,5 m² Stahloberfläche pro Liter Badlösung nur minimale Mengen in der Größenordnung von wenigen Millilitern an Badschlamm entstehen. Ein weiterer Vorteil der vorliegenden Erfindung besteht darin, daß die durch den Umsatz mit Ziehseife (Natriumstearat) entstehenden Zink-Calciumstearat-Mischseifen wegen der verbesserten Eigenschaften eine längere Standzeit der Ziehsteine ermöglichen.Another product advantage is the fact that the new zinc-calcium phosphating process for cold working works in a temperature range of preferably 50 to 70 ° C. The sludge behavior in this process can be classified as particularly favorable, since even after a bath load of 1.5 m² steel surface per liter of bath solution, only minimal quantities in the order of a few milliliters of bath sludge are produced. Another advantage of the present invention is that the Sales with drawing soap (sodium stearate) resulting zinc-calcium stearate mixed soaps allow a longer service life of the drawing dies due to the improved properties.
Es wurde eine Phosphatierungslösung hergestellt, die
10,3 g l⁻¹ Ca²⁺-Ionen
14,0 g l⁻¹ Zn²⁺-Ionen
27,8 g l⁻¹ PO₄³⁻-Ionen
46,5 g l⁻¹ NO₃⁻-Ionen
enthielt.A phosphating solution was prepared that
10.3 gl⁻¹ Ca²⁺ ions
14.0 gl⁻¹ Zn²⁺ ions
27.8 gl⁻¹ PO₄³⁻ ions
46.5 gl⁻¹ NO₃⁻ ions
contained.
Die Phosphatierlösung hatte folgende Kenndaten:
pH-Wert: ca. 2,6
Säureverhältnis: ca. 1 : 21 (freie Säure zu Gesamtsäure)The phosphating solution had the following characteristics:
pH: approx.2.6
Acid ratio: approx. 1:21 (free acid to total acid)
Stahldrähte, die zuvor mit einer alkalischen Reinigungslösung bei 80 °C während 10 Minuten durch Tauchbehandlung gereinigt und mit Wasser gespült worden waren, wurden mit der vorgenannten Phosphatierlösung 7 min bei 50 °C im Tauchen behandelt. Anschließend wurde mit Wasser gespült und eine reaktive Seife aufgetragen. Danach wurden die Drähte über Ziehsteine gezogen. Das Ergebnis war eine sehr helle und glänzende Oberfläche, die mit anderen erfindungsgemäßen Phosphatierlösungen nicht erreicht werden konnte.Steel wires which had previously been immersed in an alkaline cleaning solution at 80 ° C. for 10 minutes and rinsed with water were treated with the aforementioned phosphating solution for 7 minutes at 50 ° C. in immersion. It was then rinsed with water and a reactive soap was applied. Then the wires were drawn over drawing dies. The result was a very bright and shiny surface that could not be achieved with other phosphating solutions according to the invention.
Es wurde eine Lösung hergestellt, die
18,0 g/l Ca²⁺-Ionen
12,0 g/l Zn²⁺-Ionen
2,8 g/l Ni²⁺-Ionen
87,2 g/l PO₄³⁻-Ionen
27,5 g/l NO₃⁻-Ionen
enthielt.A solution was made that
18.0 g / l Ca²⁺ ions
12.0 g / l Zn²⁺ ions
2.8 g / l Ni²⁺ ions
87.2 g / l PO₄³⁻ ions
27.5 g / l NO₃⁻ ions
contained.
Der pH-Wert betrug 2,5 und das Verhältnis von freier
Säure zu Gesamtsäure 1 : 17,6.The pH was 2.5 and the ratio of free
Acid to total acid 1: 17.6.
Stahldraht, der vorher bei 80°C 10 Minuten lang im Tauchbad alkalisch gereinigt und anschließend kalt gespült wurde, ist mit der vorgenannten Phosphatierungslösung 10 Minuten lang bei 55°C im Tauchen behandelt worden.Steel wire, which had previously been alkaline cleaned in an immersion bath at 80 ° C. for 10 minutes and then rinsed cold, was immersed in the aforementioned phosphating solution for 10 minutes at 55 ° C.
Anschließend wurde mit Wasser gespült und im Tauchbad bei 80°C eine reaktive Ziehseife aufgebracht.It was then rinsed with water and a reactive drawing soap was applied in the immersion bath at 80 ° C.
Der so beschichtete Draht ließ sich über mehrere hintereinandergeschaltete Ziehsteine problemlos auf das Sollmaß reduzieren. Es entstand dabei eine helle und glänzende Oberfläche.The wire coated in this way could easily be reduced to the desired size using several drawing dies connected in series. The result was a bright and shiny surface.
Claims (9)
(a) 10 bis 40 g/l Ca²⁺-Ionen
(b) 10 bis 40 g/l Zn²⁺-Ionen
(c) 10 bis 100 g/l PO₄³⁻-Ionen
sowie als Beschleuniger
(d) 10 bis 100 g/l NO₃⁻-Ionen und/oder
(e) 0,1 bis 2,0 g/l organische Nitroverbindungen,
enthält,
wobei die Lösung einen pH-Wert im Bereich von 2,0 bis 3,8 und ein Verhältnis von feier Säure zu Gesamtsäure von 1 : 4 bis 1 : 100 aufweist.1. Process for phosphating metal surfaces, in particular surfaces made of iron, steel, zinc and their alloys and aluminum as a pretreatment for cold forming, the surfaces being cleaned and / or pickled in a manner known per se, characterized in that the surfaces without activation in the temperature range of 30 to 70 ° C in contact with an aqueous solution that
(a) 10 to 40 g / l Ca²⁺ ions
(b) 10 to 40 g / l Zn²⁺ ions
(c) 10 to 100 g / l PO₄³⁻ ions
as well as an accelerator
(d) 10 to 100 g / l NO₃⁻ ions and / or
(e) 0.1 to 2.0 g / l organic nitro compounds,
contains
the solution having a pH in the range of 2.0 to 3.8 and a ratio of acid to total acid of 1: 4 to 1: 100.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT89100228T ATE83509T1 (en) | 1988-01-14 | 1989-01-07 | METHOD OF PHOSPHATIONING METAL SURFACES. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3800835A DE3800835A1 (en) | 1988-01-14 | 1988-01-14 | METHOD FOR PHOSPHATING METAL SURFACES |
| DE3800835 | 1988-01-14 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0324395A1 true EP0324395A1 (en) | 1989-07-19 |
| EP0324395B1 EP0324395B1 (en) | 1992-12-16 |
Family
ID=6345237
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP89100228A Expired - Lifetime EP0324395B1 (en) | 1988-01-14 | 1989-01-07 | Process for phosphatizing metal surfaces |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US4944813A (en) |
| EP (1) | EP0324395B1 (en) |
| JP (1) | JPH01219172A (en) |
| AT (1) | ATE83509T1 (en) |
| AU (1) | AU604395B2 (en) |
| BR (1) | BR8900148A (en) |
| DE (2) | DE3800835A1 (en) |
| MX (1) | MX169762B (en) |
| TR (1) | TR26644A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006122651A1 (en) | 2005-05-19 | 2006-11-23 | Chemetall Gmbh | Method for preparing metallic workpieces for cold forming |
Families Citing this family (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5189720A (en) * | 1989-04-03 | 1993-02-23 | Sumitomo Electric Industries, Ltd. | Method for manufacturing steel wire material for reinforcing optical fiber |
| JPH03215684A (en) * | 1990-01-18 | 1991-09-20 | Nippon Parkerizing Co Ltd | Lubricating film treatment for aluminum |
| DE4029985A1 (en) * | 1990-09-21 | 1992-03-26 | Bohnacker Tegometall | METHOD FOR POWDER COATING METAL SURFACES |
| DE19634685A1 (en) * | 1996-08-28 | 1998-03-05 | Metallgesellschaft Ag | Aqueous solution and process for phosphating metallic surfaces |
| US5968240A (en) * | 1997-08-19 | 1999-10-19 | Sermatech International Inc. | Phosphate bonding composition |
| DE19808440C2 (en) * | 1998-02-27 | 2000-08-24 | Metallgesellschaft Ag | Aqueous solution and method for phosphating metallic surfaces and use of the solution and method |
| JP2000119862A (en) * | 1998-10-07 | 2000-04-25 | Nippon Parkerizing Co Ltd | Lubrication method for cold plastic working of steel |
| RU2160324C1 (en) * | 1999-03-11 | 2000-12-10 | Закрытое акционерное общество "Мультисервис" | Composition for protection from corrosion of ferrous metal surfaces |
| US6902766B1 (en) | 2000-07-27 | 2005-06-07 | Lord Corporation | Two-part aqueous metal protection treatment |
| RU2174161C1 (en) * | 2000-10-30 | 2001-09-27 | Танасиенко Сергей Юрьевич | Anticorrosive composition and method of its application to metal surface |
| CN100374620C (en) | 2002-07-10 | 2008-03-12 | 坎梅陶尔股份有限公司 | Coating methods for metal surfaces |
| DE10320313B4 (en) * | 2003-05-06 | 2005-08-11 | Chemetall Gmbh | A method of coating metallic bodies with a phosphating solution, phosphating solution and the use of the coated article |
| DE10323305B4 (en) * | 2003-05-23 | 2006-03-30 | Chemetall Gmbh | Process for coating metallic surfaces with a phosphating solution containing hydrogen peroxide, phosphating solution and use of the treated articles |
| JP5153063B2 (en) * | 2005-07-15 | 2013-02-27 | 日本発條株式会社 | Steel surface treatment method |
| JPWO2007026756A1 (en) * | 2005-08-31 | 2009-03-12 | アイシン・エィ・ダブリュ株式会社 | Manufacturing method of annular member and annular member with legs |
| JP6879090B2 (en) * | 2017-07-07 | 2021-06-02 | 三菱瓦斯化学株式会社 | Method for manufacturing rolls and sheet molded products for melt extrusion |
| EP4121580A1 (en) * | 2020-03-19 | 2023-01-25 | ThyssenKrupp Steel Europe AG | Method for generating a phosphate conversion coating and nickel-free phosphating solution |
| EP3964606A1 (en) * | 2020-09-04 | 2022-03-09 | Henkel AG & Co. KGaA | Single stage zinc phosphating method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2540685A1 (en) * | 1975-09-12 | 1977-03-17 | Metallgesellschaft Ag | PROCESS FOR PRODUCING PHOSPHATE COATINGS ON METAL SURFACES |
| US4622078A (en) * | 1984-03-01 | 1986-11-11 | Gerhard Collardin Gmbh | Process for the zinc/calcium phosphatizing of metal surfaces at low treatment temperatures |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3090709A (en) * | 1953-08-10 | 1963-05-21 | Lubrizol Corp | Phosphate coating of metals |
| US3161549A (en) * | 1955-04-08 | 1964-12-15 | Lubrizol Corp | Solution for forming zinc phosphate coatings on metallic surfaces |
| US3104177A (en) * | 1961-12-12 | 1963-09-17 | Lubrizol Corp | Phosphating process |
| JPS5558376A (en) * | 1978-10-21 | 1980-05-01 | Nippon Paint Co Ltd | Calsium modified zinc phosphate film treating solution |
| GB2080835B (en) * | 1980-07-25 | 1984-08-30 | Pyrene Chemical Services Ltd | Prevention of sludge in phosphating baths |
| JPS60204890A (en) * | 1984-03-28 | 1985-10-16 | Nippon Parkerizing Co Ltd | Phosphate treatment method for steel wire rod |
| DE3571562D1 (en) * | 1984-05-21 | 1989-08-24 | Sumitomo Metal Ind | Method for continuous drawing of wire rod |
| CA1257527A (en) * | 1984-12-20 | 1989-07-18 | Thomas W. Tull | Cold deformation process employing improved lubrication coating |
-
1988
- 1988-01-14 DE DE3800835A patent/DE3800835A1/en not_active Withdrawn
-
1989
- 1989-01-07 DE DE8989100228T patent/DE58902980D1/en not_active Expired - Fee Related
- 1989-01-07 EP EP89100228A patent/EP0324395B1/en not_active Expired - Lifetime
- 1989-01-07 AT AT89100228T patent/ATE83509T1/en not_active IP Right Cessation
- 1989-01-12 TR TR89/0045A patent/TR26644A/en unknown
- 1989-01-13 BR BR898900148A patent/BR8900148A/en unknown
- 1989-01-13 US US07/297,155 patent/US4944813A/en not_active Expired - Fee Related
- 1989-01-13 AU AU28508/89A patent/AU604395B2/en not_active Ceased
- 1989-01-13 MX MX014531A patent/MX169762B/en unknown
- 1989-01-17 JP JP1009621A patent/JPH01219172A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2540685A1 (en) * | 1975-09-12 | 1977-03-17 | Metallgesellschaft Ag | PROCESS FOR PRODUCING PHOSPHATE COATINGS ON METAL SURFACES |
| US4622078A (en) * | 1984-03-01 | 1986-11-11 | Gerhard Collardin Gmbh | Process for the zinc/calcium phosphatizing of metal surfaces at low treatment temperatures |
Non-Patent Citations (1)
| Title |
|---|
| PATENT ABSTRACTS OF JAPAN, Unexamined Applications, Sektion C, Band 4,Nr. 98, 15. Juli 1980 The Patent Office Japanese Government seite 8 C 18 Kokai-Nr. 55-58 376 (Nippon Paint K.K.) * Gesamt * * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006122651A1 (en) | 2005-05-19 | 2006-11-23 | Chemetall Gmbh | Method for preparing metallic workpieces for cold forming |
| EA012533B1 (en) * | 2005-05-19 | 2009-10-30 | Шеметалл Гмбх | Method for preparing metallic workpieces for cold forming |
Also Published As
| Publication number | Publication date |
|---|---|
| DE58902980D1 (en) | 1993-01-28 |
| ATE83509T1 (en) | 1993-01-15 |
| AU2850889A (en) | 1989-07-20 |
| BR8900148A (en) | 1989-09-12 |
| US4944813A (en) | 1990-07-31 |
| TR26644A (en) | 1994-05-25 |
| AU604395B2 (en) | 1990-12-13 |
| JPH01219172A (en) | 1989-09-01 |
| EP0324395B1 (en) | 1992-12-16 |
| DE3800835A1 (en) | 1989-07-27 |
| MX169762B (en) | 1993-07-23 |
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