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
  • C23C22/68—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 solutions with pH between 6 and 8
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
  • C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
  • C25D11/02—Anodisation
  • C25D11/34—Anodisation of metals or alloys not provided for in groups C25D11/04 - C25D11/32
• • C—CHEMISTRY; METALLURGY
  • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
  • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
  • C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
  • C25D5/48—After-treatment of electroplated surfaces
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/12—All metal or with adjacent metals
  • Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
  • Y10T428/12535—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.] with additional, spatially distinct nonmetal component
  • Y10T428/12583—Component contains compound of adjacent metal
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/12—All metal or with adjacent metals
  • Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
  • Y10T428/12771—Transition metal-base component
  • Y10T428/12785—Group IIB metal-base component
  • Y10T428/12792—Zn-base component
  • Y10T428/12799—Next to Fe-base component [e.g., galvanized]

Definitions

• Galvanized steel sheets coated with a pre-lubricating layer of hydroxysulfate and methods of obtaining this sheet are coated with a pre-lubricating layer of hydroxysulfate and methods of obtaining this sheet.
• the invention relates to the pre-lubrication of the zinc-coated surface of sheets coated with zinc or a zinc-based alloy and the treatment of these sheets in aqueous solutions containing sulphates.
• the concentration of Zn (OH) 4 ions reaches the solubility product, the zinc hydroxide Zn (OH) 2 precipitates and forms a passivating film on the surface.
• this document (see page 115) also teaches that an excessively high concentration of anions in the alkaline solution causes the passivation film formed after the first oxidation step to rupture.
• the area of concentration studied in this document covers the range
• Documents JP 61-60915, 63-46158, 63-46159 and EP 0 339 578 describe anodic treatments of zinc-plated steel sheets in aqueous solutions containing sulfates and the use of these treatments to color the zinc-coated surfaces of these sheets.
• the concentration of electrolyte in the treatment solution is between 70 and 200 g / 1; the concentration of sodium sulphate is for example 150 g / l, that is to say about 1 mole / liter.
• Document JP 63-274797 describes the use of a treatment of the same type to improve the ability to phosphatize steel sheets coated by electrodeposition of a zinc-based alloy containing nickel.
• the treatment solution then contains, in addition to the sulphates (for example: magnesium, sodium or aluminum sulphate at 150 g / l), carboxylic acids (for example: citric, maleic, salicylic at 30 or 40 g / l ).
• the pH of the treatment solution is between 4 and 5.5.
• the anodic treatment is carried out at a current density of between 30 and 200 A / dm 2 until the quantity of electricity consumed is between 50 and 500 C / dm 2 of surface to be treated.
• this treatment improves the aptitude for phosphating because it results in the elimination of the surface traces of zinc hydroxides - Zn (OH) 2 - and makes it possible to improve the surface reactivity.
• Patent EP 0 489 105 describes a method for treating the metal surface of a sheet, in particular a steel sheet, intended to prepare said sheet for stamping and / or to protect it against corrosion, in which :
• At least one oiling operation is carried out on said surface.
• the application and drying conditions are suitable for obtaining a phosphate deposit with a surface density of between 5 to 40 mg / m 2 .
• the oil used can be a temporary protection oil against corrosion and / or a lubricating oil for shaping, in particular drawing.
• a first protective oiling can be carried out; after destocking, a second lubrication oiling can be carried out to prepare the shaping, in particular by stamping.
• the phosphating treatment prior to oiling, makes it possible to substantially improve the lubrication at the time of shaping: it is therefore a pre-lubrication treatment.
• the galvanized sheet obtained has a pre-lubricating deposit based on phosphate.
• the object of the invention is to provide a pre-lubricated galvanized sheet which is more efficient than those obtained by phosphating and to offer a pre-lubrication treatment for galvanized sheets which is more effective than a phosphating treatment and more respectful of the environment. of the effluents it generates.
• the subject of the invention is a steel sheet coated with a metallic layer based on zinc, characterized in that:
• said metallic layer is itself coated with a layer based on zinc hydroxysulfate,
• the surface density of sulfur corresponding to said hydroxysulfate layer is greater than 0.5 mg / m 2 .
• the invention therefore also relates to a first method for obtaining a sheet according to the invention from a steel sheet coated with a metallic layer based on zinc comprising the steps consisting in applying to the surface galvanized from the starting plate an aqueous treatment solution containing more than 0.07 moles of sulfate ions per liter, to be polarized so anodic said surface so as to circulate a bias current, then rinse said surface, then dry it, characterized in that:
• the pH of said solution is greater than or equal to 12, and less than 13.
• the quantity of electric charges, circulating during the treatment through said surface and generating on said surface the deposition of a layer comprising sulfur, is adapted so that the quantity of sulfur obtained in said hydroxysulfate layer exceeds 0.5 mg / m 2 .
• the pre-lubricating effect obtained is greater than that provided by a treatment in a phosphate solution as described in EP 0 489 105.
• this layer of zinc hydroxysulfate should adhere to the treated surface: the conditions relating to the pH of the treatment solution and the drying step at the end of treatment are decisive for this effect. If the pH of the solution is less than 12, no adherent hydroxysulfates are formed on the surface to be treated; if the pH of the solution is greater than or equal to 13, the hydroxysulfate redissolves and / or decomposes into zinc hydroxides; we then find us in conditions analogous to those described in the document by SS Abd El Rehim previously cited.
• the layer deposited on the sheet After rinsing but before drying, the layer deposited on the sheet has the appearance of a gel which is still not very adherent; the drying is adapted to remove the residual liquid water from the deposit and allows the layer to adhere better to the sheet.
• sodium sulfate is used in the solution, if the sodium sulfate concentration is less than 10 g / l in the solution, little formation of hydroxysulfate layer is observed on the surface; more generally, it is therefore important that the concentration of sulfate ions be greater than 0.07 moles per liter.
• the pre-lubricating effect of the hydroxysulfate layer was found to decrease if the quantity of sulfur deposited greatly exceeded 30 mg / m 2 , apparently due to the degradation of the adhesion of this layer; it has also been found that if the quantity of sulfur deposited exceeds 27 mg / m 2 , the phosphatability of the sheet obtained degrades, the phosphate crystals deposited then being too large.
• the quantity of hydroxysulfates deposited should be greater than 0.5 mg / m 2 and less than or equal to 30 mg / m 2 in sulfur equivalent, preferably between 3.5 and 27 mg / m 2 in sulfur equivalent.
• the charge density applied should therefore be adapted to this quantity of hydroxysulfates capable of providing this significant prelubricating effect.
• the charge density applied is preferably between 10 and 100 C / dm 2 of surface to be treated. If the charge density exceeds 100 C / dm 2 , it can be seen that the quantity of sulfur deposited on the surface no longer increases and even decreases.
• This first process for obtaining a sheet according to the invention therefore makes it possible to form on a zinc-plated surface a layer based on hydroxysulfate, which is both sufficiently thick and adherent. Thanks to the anodic polarization of the zinc-plated surface to be treated, there is a rapid dissolution of the zinc in the immediate vicinity of the zinc-plated surface, which promotes the precipitation of zinc salts on this surface.
• a titanium cathode As a counter electrode, a titanium cathode can be used.
• the temperature of the treatment solution is generally between 20 ° C and 60 ° C; preferably, a temperature greater than or equal to 40 ° C. is carried out, so as to increase the conductivity of the solution and to reduce the ohmic losses.
• the speed of circulation of the solution on the surface of the sheet has no decisive impact on the treatment according to the invention.
• the treated surface is thoroughly rinsed with demineralized water; in this first process, the rinsing step is important to remove the alkaline reagents on the surface of the deposit, which would cause corrosion problems.
• the sheet thus pre-lubricated by the treatment according to the invention has a homogeneous coloring, a little more sustained compared to that of an untreated galvanized sheet; this treatment does not, however, color the sheet, as in documents JP 61-60915, 63-46158, 63-46-159 and EP 0 339 578 already cited; observed under the microscope, the deposit resulting from the treatment according to the invention is in the form of scattered plaques; it has been observed that the density of plates increases with the quantity of sulfur deposited per unit of area.
• the zinc necessary for the formation of the pre-lubricating deposit of zinc hydroxysulfate comes from the anodic dissolution of the zinc under the effect of the polarization of the zinc-plated surface. .
• This first production process obviously has the economic disadvantage of requiring a polarization installation.
• the invention also relates to a second process for obtaining a sheet according to the invention from a steel sheet coated with a metallic layer based on zinc comprising:
• said treatment solution contains Zn 2+ ions at a concentration greater than 0.01 mole / liter
• Other advantageous characteristics of the second process for obtaining the sheet according to the invention are indicated in the dependent claims.
• This second method of obtaining a sheet according to the invention does not require a polarization installation.
• the pH of the treatment solution used for this second process is generally much less basic than that of the treatment solution used for the first process; the pH of the treatment solution preferably corresponds to the natural pH of the solution, without addition of base or acid; the value of this pH is generally between 5 and 7.
• the treatment solution is applied to a galvanized sheet metal surface in a conventional manner, for example by dipping, spraying or coating.
• the treatment solutions used contain between 20 and
• the sheet is preferably rinsed so as to remove the soluble part of the deposit obtained; the absence of rinsing and the obtaining of a deposit which is partially soluble in water which results therefrom are not very detrimental to the prelubricating effect, provided that the deposit obtained clearly includes the prelubricating layer of hydroxysulfate insoluble in l water in contact with the sheet.
• the conditions of application of the solution > the duration of application: the deposit obtained after 300 seconds may have a surface density twice that obtained after
• the temperature of the treatment solution the optimum temperature range is determined, for example between 40 ° C and 60 ° C.
• concentrations of SO 4 ions and ions
• the treatment solution contains an oxidizing agent for zinc, such as hydrogen peroxide; this oxidizing agent can have a very marked hydroxysulfation accelerating effect at low concentration; it was found that the addition of only 0.03%, or 8 10 " 3 mole / liter of hydrogen peroxide, or of 2 10" 4 mole / liter of potassium permanganate in the solution made it possible to double (approximately) the filing speed; on the contrary, it has been found that concentrations 100 times greater no longer make it possible to obtain this improvement in the deposition rate.
• an oxidizing agent for zinc such as hydrogen peroxide
• this oxidizing agent can have a very marked hydroxysulfation accelerating effect at low concentration
• the invention finally relates to a process for shaping a steel sheet coated with a metallic layer based on zinc comprising the steps consisting in treating the surface of said coated sheet according to the first or second process described above, applying a film of lubricating oil to said dried treated surface and shaping said sheet properly.
• These processes apply for example on electro-galvanized sheets; for hot dip galvanized sheets, the second treatment process should preferably be used; for sheets coated with zinc alloy, the second treatment process without rinsing will be used, for example.
• FIG. 3 and 4 show the infrared reflection spectra of sheets coated with a layer of hydroxysulfate according to the invention, respectively according to the first and according to the second methods of obtaining this sheet previously described.
• the sheet used for the treatment tests is a sheet of steel, grade known as “aluminum calmed steel” of ES quality, 0.7 mm thick, coated by electrodeposition in chloride bath on both sides. '' a metallic layer of zinc about 7.5 ⁇ m thick.
• the sulfate used to prepare the treatment solution for the first process is sodium sulfate; any other soluble sulfate can be used.
• the sulfate used for the second process according to the invention is zinc sulfate heptahydrate ZnSO 4 , 7 H 2 O.
• stamping press adapted to produce buckets with an inside diameter of 50 mm from sheet blanks with a diameter of 90 mm; using a 50 mm diameter punch having at the end a radius of curvature of 3 mm, a 52.6 mm diameter die having an inner rim of radius of curvature 3.5 mm.
• the drawing speed is set at 12 cm / min. ; the maximum force of hold-down is 150 kN.
• the press is equipped with means for continuously monitoring the drawing parameters, in particular the blank holding pressure, the drawing force and the stroke of the punch.
• the curve of the drawing force is plotted as a function of the stroke of the punch; this curve passes through a maximum which defines the maximum drawing force during operation.
• This drawing test protocol therefore makes it possible to assess the level of lubrication of the surface of a sheet for drawing; to assess this level on one side, a film of Teflon ® (punch side) is affixed to the other side so as to obtain on this other side a friction which is always constant with regard to that which is exerted on the surface to be evaluated .
• this protocol is applied to pre-lubricated sheets by prior treatment and oiled in a standard manner (with Teflon® film on the untreated side ); standard oiling here consists in applying, to the treated surface, oil referenced 6130 from the company QUAKER so as to obtain a layer of approximately 1 g / m 2 .
• the sheet metal samples are phosphated according to a predetermined protocol corresponding to conventional methods practiced in the automotive industry, using several conventional surface treatment baths adapted to form a layer of zinc, manganese and nickel phosphates; baths sold for this purpose by the PARKER or CFPI companies can be used; generally and successively, one or two alkaline degreasing baths are used, a refining bath, then a phosphating bath; each step is followed by a water rinse.
• the quality of the layer of deposited phosphates is evaluated, in particular in terms of morphology and chemical composition; scanning electron microscopy and atomic absorption spectroscopy are used for this purpose.
• the sheet metal samples are processed in a “cell with electrolyte circulation” where they are immersed in this solution brought to 40 ° C., and where they are anodically polarized with respect to a titanium cathode; the “electrolyte circulation cell” is adjusted so that the speed of the electrolyte in the vicinity and along the surface of the sheet to be treated is 100 m / min.
• the surface of the samples is then analyzed so as to measure the quantity of sulfur deposited on the surface; the amount of sodium on the surface is also measured; the results are shown in Table I.
• the sulfur is determined by X-ray fluorescence ("SFX"); the depth taken into account by this analysis method is several microns; as the zinc-plated steel substrate does not contain sulfur (apart from the quantities corresponding to unavoidable impurities), the signal given by this assay method then effectively corresponds to sulfur deposited during the treatment; the quantity of sulfur deposited is calculated from the measured signal, according to a pre-established law.
• SFX X-ray fluorescence
• the sodium is measured, after leaching the surface with boiling water, by atomic absorption spectroscopy ("AAS").
• AAS atomic absorption spectroscopy
• Example 1 On the same sheet samples as in Example 1, a comparative treatment was carried out under anodic polarization (charge density: 12 C / dm 2 - current density: 9.8 A / dm 2 ) in a solution at same temperature and at the same pH as in Example 1, but not containing sulfates; this comparative treatment therefore consists in depositing a layer of zinc hydroxides in place of the hydroxysulfates of Example 1.
• the low level of current density used comes from the low level of conductivity of the electrolyte used which contains only welded.
• Rotating electrode cell the circular shaped sample is immersed in this cell and is rotated; the running speed of the electrolyte in the vicinity of the sample therefore depends on the speed of rotation.
• Example 1 A series of treatments is carried out on the same samples as in Example 1 and using a solution similar to that of Example 1, except for the pH value; the treatment installation is the same as in Example 2 (“cell with rotating electrode”). All the treatments are carried out under the same charge density 20 C / dm 2 and under the same current density 200 A / dm 2 .
• Each treatment is carried out using a solution of different pH; after treatment, the quantity of sulfur deposited is measured by the same method as in Example 2.
• the quantity of sulfur deposited becomes significant, that is to say greater than 0.5 mg / m 2 only if, approximately, 12 ⁇ pH ⁇ 13.
• the amount of sulfur is less than 1 mg / m 2 , which shows that the hydroxysulfate deposit is eliminated during phosphating.
• painted sheets After phosphating and painting of treated sheets according to tests No. 2 and No. 3 of Example 1, painted sheets are obtained having as good a surface appearance as the reference sheet phosphated and painted under the same conditions.
• a treatment solution is prepared by dissolving zinc sulfate heptahydrate in water; the solution is used at its natural pH, without addition of acid or base; the natural pH obtained is close to 7.
• the sheet samples are soaked in this solution, without electrical polarization. After immersion, the treated samples are rinsed twice with demineralized water: first at 20 ° C for approximately 8 seconds, then at 50 ° C for approximately 5 seconds.
• the rinsed samples are then dried. A deposition of hydroxysulfate is observed on the samples obtained; due to rinsing, it is therefore considered that the deposits obtained are insoluble in water.
• a treatment solution is prepared by dissolving 25.7 g / l of zinc sulphate heptahydrate in water; the solution is used at its natural pH, without addition of acid or base; the natural pH obtained is close to 7.
• a homogeneous film of treatment solution is applied by coating the sheet metal samples; the solution is applied at room temperature. 5 to 60 seconds after application, the sample is dried. The deposits obtained on the dried samples then all have the same thickness and the same amount of sulfur.
• the solubiiisable part of the deposit depends on the time (5 to 60 seconds) between application and drying, during which the hydroxysulfation reaction may have developed.
• the quantity of sulfur corresponding to the soluble part of the deposit and that corresponding to the insoluble part, that is to say to the hydroxysulfate, are measured.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Electrochemistry (AREA)
• General Chemical & Material Sciences (AREA)
• Mechanical Engineering (AREA)
• Chemical Treatment Of Metals (AREA)
• Laminated Bodies (AREA)
• Lubricants (AREA)
• Electroplating Methods And Accessories (AREA)
• Paper (AREA)
• Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)

Applications Claiming Priority (3)

Publications (2)

Family

ID=9530403

Family Applications (1)

Country Status (10)

Cited By (1)

Families Citing this family (15)

Family Cites Families (4)

• 1998
  • 1998-09-15 US US09/786,984 patent/US6528182B1/en not_active Expired - Lifetime
  • 1998-09-15 FR FR9811441A patent/FR2783256B1/fr not_active Expired - Fee Related
• 1999
  • 1999-09-09 PT PT99941724T patent/PT1115914E/pt unknown
  • 1999-09-09 BR BRPI9913743-7A patent/BR9913743B1/pt not_active IP Right Cessation
  • 1999-09-09 ES ES99941724T patent/ES2196847T3/es not_active Expired - Lifetime
  • 1999-09-09 DE DE69906555T patent/DE69906555T2/de not_active Expired - Lifetime
  • 1999-09-09 CA CA2343016A patent/CA2343016C/fr not_active Expired - Lifetime
  • 1999-09-09 AT AT99941724T patent/ATE236279T1/de active
  • 1999-09-09 EP EP99941724A patent/EP1115914B1/de not_active Expired - Lifetime
  • 1999-09-09 WO PCT/FR1999/002141 patent/WO2000015878A1/fr active IP Right Grant

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events