WO2019121582A1 - Procédé pour fabriquer un fer noir revêtu de chrome-oxyde de chrome - Google Patents

Procédé pour fabriquer un fer noir revêtu de chrome-oxyde de chrome Download PDF

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Publication number
WO2019121582A1
WO2019121582A1 PCT/EP2018/085335 EP2018085335W WO2019121582A1 WO 2019121582 A1 WO2019121582 A1 WO 2019121582A1 EP 2018085335 W EP2018085335 W EP 2018085335W WO 2019121582 A1 WO2019121582 A1 WO 2019121582A1
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WIPO (PCT)
Prior art keywords
chromium
chromium oxide
coating
metal
iii
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PCT/EP2018/085335
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English (en)
Inventor
Jacques Hubert Olga Joseph Wijenberg
Adrianus Jacobus Wittebrood
Mark Willem LITZ
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Tata Steel Ijmuiden B.V.
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Publication date
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Priority to EP18829799.8A priority Critical patent/EP3728701A1/fr
Publication of WO2019121582A1 publication Critical patent/WO2019121582A1/fr

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/04—Electroplating: Baths therefor from solutions of chromium
    • C25D3/06—Electroplating: Baths therefor from solutions of chromium from solutions of trivalent chromium
    • 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
    • C25D5/18—Electroplating using modulated, pulsed or reversing current
    • 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
    • C25D5/627—Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00—Electroplating characterised by the article coated
    • C25D7/06—Wires; Strips; Foils
    • C25D7/0614—Strips or foils
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D9/00—Electrolytic coating other than with metals
    • C25D9/04—Electrolytic coating other than with metals with inorganic materials
    • C25D9/08—Electrolytic coating other than with metals with inorganic materials by cathodic processes
    • C25D9/10—Electrolytic coating other than with metals with inorganic materials by cathodic processes on iron or steel

Definitions

  • This invention relates to a method for electroplating an uncoated steel strip with a plating layer and an improvement thereof.
  • a cold-rolled steel strip is provided which is usually annealed after cold-rolling to soften the steel by recrystallisation annealing or recovery annealing. After the annealing and before plating the steel strip is first cleaned for removing oil and other surface contaminants. After the cleaning step, the steel strip is pickled in a sulphuric or hydrochloric acid solution for removing the oxide film. Between different treatment steps the steel strip is always rinsed with deionised water to prevent contamination of the solution used for the next treatment step with solution of the preceding treatment step. Consequently the steel strip is thoroughly rinsed after the pickling step. During rinsing and transport of the steel strip to the plating section a fresh thin oxide layer is formed instantly on the bare steel surface and needs to be protected quickly.
  • the part to be plated (the steel strip) is the cathode of the circuit.
  • the anode of the circuit may be made of the metal to be plated on the part (dissolving anode, such as those used in conventional tinplating) or a dimensionally stable anode (which does not dissolve during plating).
  • the anode and cathode are immersed in an electrolyte solution containing ions of the metal to be deposited onto the blackplate substrate.
  • Blackplate is a tin mill product which has not (yet) received any metallic coating during production. It is the basic material for the production of other tin mill products. Blackplate can be single reduced (SR) full-hard or annealed (recovery annealed or recrystallisation annealed) or double reduced (DR) in which case it has been subjected to a second cold rolling reduction after annealing.
  • the SR or DR blackplate is usually provided in the form of a coiled strip and is the uncoated starting material for the coating process according to the invention.
  • Figure 1 schematically summarises the process steps to obtain the coated product, starting from a hot-rolled strip. Before cold-rolling, the hot-rolled strip is usually pickled (not shown) to remove the hot-rolling scale and cleaned (not shown) to remove any contaminants from the strip.
  • the coated product performs just as well in terms of corrosion performance, coatability, adherence of the lacquer coating or polymer coating to the coated product and the can-making performance of the coated product, no adverse effects have been observed of the presence of the stripes, the stripy appearance is considered to be visually less appealing and therefore undesired.
  • WO2015177314-A1 discloses a method for producing a steel substrate coated with a chromium metal-chromium oxide (Cr-CrOx) coating layer in a continuous high speed plating line, operating at a line speed of at least 100 m/min, wherein one or both sides of the electrically conductive substrate in the form of a strip, moving through the line, is coated with a chromium metal-chromium oxide (Cr-CrOx) coating layer from a single electrolyte by using a plating process.
  • the object is reached with a method for manufacturing a chromium metal - chromium oxide coated blackplate by electrolytically depositing the chromium metal - chromium oxide coating on blackplate in a continuous high speed plating line operating at a line speed of at least 50 m/min from an electrolyte solution comprising a trivalent chromium compound, wherein the electrolyte solution is free of chloride ions and of a boric acid buffering agent, the electrically conductive substrate acts as a cathode and an anode comprising a catalytic coating of iridium oxide or a mixed metal oxide for reducing or eliminating the oxidation of Cr 3+ -ions to Cr 6+ -ions, wherein the electrolyte solution contains at most 250 mM Cr 3+ -ions, a complexing agent at a molar ratio of at least 1 : 1, 0 to 2800 mM of sodium sulphate (Na 2 S0 4 ), a pH of between 1.5 and 3.0
  • the first chromium metal - chromium oxide coating may consist of several identical layers on top of each other. These layers are not discernible from each other.
  • the first chromium metal - chromium oxide coating and the second chromium metal - chromium oxide coating are discernible from each other because the oxide content of the second chromium metal - chromium oxide coating is significantly higher than that of the first.
  • the effect of this method is that the resulting coated blackplate has a better adhesion to an organic coating and the surface is shiny and shows no stripy appearance from an electrolyte with a reduced amount of trivalent chromium compound.
  • the ever increasing demands in terms of adhesion is thereby met.
  • the method according to the invention can be used in a plating line consisting one or more plating cells each comprising one or more anodes.
  • the requirement is that the anodes can be controlled in terms of current. If the plating line consists of only one plating cell with a plurality of individually controllable anodes then the first chromium metal - chromium oxide coating will be deposited using the first anode(s) and the second chromium metal - chromium oxide coating will be deposited using later anode(s).
  • the optional currentless part can be the part of the plating cells where the anodes are currentless, or it can be in between two plating cells, or it can be a currentless intermediate plating cell. The important part is that the first part of the plating process is executed under regime II conditions, and the second part under regime III (preferably regime Illb) conditions, with an optional currentless interruption in between.
  • the continuous high speed plating line consists of a sequence of N plating cells (CI ..C N ) each of which has individual current control, wherein the deposition of the first chromium metal - chromium oxide coating at the first current density (i reg ime n) is performed in one or more of the first anodes of the plating line, optionally followed by a currentless period, followed by the deposition of the second chromium metal - chromium oxide coating at the second current density (i re gime m) in the last anode or anodes of the plating line.
  • this finding is not limited to the tested situation in which there are 5 plating cells each with one or more anodes, but that this finding is equally valid for plating lines with 3 or 4 and more than 5. It is important that the cells or the anodes in the cells can be controlled individually as to the imposed current.
  • the chromium oxide in the second chromium metal - chromium oxide coating is between 4 and 24 mg/m 2 , preferably between 6 and 18 mg/m 2 , more preferably between 6 and 15 mg/m 2 , and most preferably between 8 and 15 mg/m 2 .
  • the inventors found that it is preferable that the chromium oxide in the first chromium metal - chromium oxide coating is below 6 mg/m 2 , preferably below 4 mg/m 2 , more preferably below 3 mg/m 2 , and most preferably below 2 mg/m 2 .
  • the molar ratio is expressed as follows:
  • the deposition mechanism of the chromium layer from the electrolyte solution according to the invention is assumed to be based on a fast, stepwise deprotonation of the water ligands in the Cr 3+ -formate complex ion induced by a surface pH increase as a result of hydrogen evolution (2H + + 2e H 2 (g)) (See Figure 3 and 4A and 4B):
  • the chromium metal - chromium oxide always also contains Cr-carbide.
  • the amount was found to be relatively independent of the deposition process. It is believed that the origin of the carbon in the carbide is the formate ion complexing agent. So even though carbide is not mentioned explicitly herein above and below as a constuent of the chromium metal - chromium oxide, it is present. Values of between 5 and 25% of the total chromium content can be present as Cr-carbide.
  • minute amounts of Cr-sulphate of up to several percents may be incorporated in the chromium metal - chromium oxide layer.
  • the chromium oxide (and the Cr-carbide and Cr-sulphate (if present)) is more or less uniformly distributed in the Cr-metal. This applies to the first (regime II) layer(s) and to the second (regime III) layers.
  • regime II See Figure 4A
  • a mixed Cr-metal-carbide-oxide coating is deposited on the steel substrate.
  • regime III there is no deposition of chromium, and in regime III the amount of deposited chromium drops sharply.
  • regime III is split in two, indicated with the dashed lines which shows a sharp drop (regime Ilia) to a plateau value (regime Illb). From a plating and process control perspective the deposition of the second chromium metal - chromium oxide coating at a higher second current density is preferably performed in regime Illb.
  • the current density at which the desired chromium coating weight and composition are obtained depends on the electrolyte composition, pH, temperature and mass transfer rate (strip speed in case of a strip plating line).
  • the optimal current density is not a discrete value, but a range of values restricted by a lower and an upper limit. This current density range is called the 'plating window'. Within the plating window, the coating properties fall within certain specifications. From an operational perspective, a large plating window is desired, because this simplifies process control.
  • the method according to the invention is based on the combination of first depositing a Cr-metal-carbide-oxide coating on the blackplate substrate under the regime II conditions, followed by depositing a Cr-metal-carbide-oxide coating on the blackplate substrate under the regime III conditions.
  • the process according to the invention is equally applicable to provide a chromium metal-chromium oxide coating on other metal substrates such as nickel plated steel strip.
  • sulphuric acid or sodium hydroxide may be added to adjust the pH to a value inside the desired range.
  • acids or bases may be used, but in view of the bath chemistry sulphuric acid and sodium hydroxide are preferable.
  • any steel grade suitable for producing packaging steel may be used.
  • a stripy appearance of a deposited surface is usually associated with a certain inhomogeneity in the electroplating process.
  • a local difference in coverage or local differences in the composition of the coating layer may be the cause of the stripy appearance. It would be obvious to the skilled person to attempt to solve this problem by increasing the amount of deposited material by either increasing the amount of metal ions in the electrolyte, or by increasing the current density.
  • the inventors found that by increasing the chromium(III) content in the electrolyte, the appearance of the coated strip worsened, and that the stripy appearance persisted. Surprisingly and counter-intuitively the inventors found that decreasing the amount of metal ions in the electrolyte resulted in a decrease in the stripy surface and that the surface becomes even and shiny when the coating was deposited in accordance with the process of the invention.
  • FIG. 2A The effect of a lower chromium content in the electrolyte solution is shown in Figure 2A.
  • Figure 2B the Cr weight is plotted as a function of current density. All curves show the typical features that can be associated with the 3 different regimes as outlined in the introduction.
  • the Cr content is lowered from 20 to 10 g/l the same Cr coating weight is obtained at a lower current density (regime II is shifted to the left), because less OH- is required for converting less [Cr(HC00)(H 2 0) 5 ] 2+ to Cr(HC00)(0H) 2 (H 2 0) 3 .
  • the maximum Cr coating weight (transition from regime II to III) is about halved when the Cr content is lowered from 20 to 10 g/l.
  • the maximum Cr coating weight strongly increases when the pH is lowered.
  • the various Cr(III) formate complex ion species as depicted in Figure 3 will coexist at a given pH.
  • the pH gradient along the diffusion boundary layer will be steeper for a lower bulk pH. Consequently, the distribution of the various species not only depends on the surface pH, but also on the bulk pH.
  • the complexing agent is formate (HCOO ), added to the electrolyte solution preferably as sodiumformate (HCOONa).
  • formate HCOO
  • HCOONa sodiumformate
  • complexing agents that can be used instead of formate, or in addition thereto are oxalate-ions, and acetate-ions.
  • the Cr 3+ -ions are provided by a water soluble chromium(III) salt and wherein the water soluble chromium(III) salt preferably is one or more of the following water soluble chromium(III) salts:
  • the electrolyte solution contains at most 225 mM of Cr 3+ -ions and/or at least 100 mM of Cr 3+ -ions, preferably at least 125 mM of Cr 3+ -ions.
  • This preferred range provides good results with regard to appearance, particularly relevant for the first chromium metal - chromium oxide coating (deposited in regime II) and good adherence with regard to lacquers particularly relevant for the second chromium metal - chromium oxide coating (deposited in regime III).
  • the pH of the electrolyte solution is at most 2.8 (i.e. £ 2.8), preferably at most 2.6 or 2.4, more preferably at most 2.2.
  • £ 2.8 i.e. £ 2.8
  • the surface quality is much improved in that it shows no stripes.
  • the formate/Cr 3+ molar ratio is at most 2.5: 1.
  • the formate-ion is needed as a complexing agent and the ratio of at most 2.5: 1 has proven to be sufficient in most cases.
  • the molar ratio is at most 2.0: 1, even more preferably 1.75: 1.
  • the molar ratio is at least 1.1 : 1, more preferably 1.25: 1.
  • the electrolyte solution contains at least 75 mM and/or at most 600 mM of sodium formate.
  • at least 75 mM should be added, preferably at least 100 mM and even more preferably 200 mM.
  • the maximum is preferably at most 600 mM of sodium formate. If also chromium(III)formate is added to the electrolyte solution as the water soluble chromium salt then the formate added this way needs to be subtracted from the sodium formate additions as given herein above.
  • the values for sodium formate become at least 25 mM, preferably at least 50 mM and even more preferably 150 mM.
  • the maximum is preferably at most 550 mM of sodium formate.
  • the electrolyte solution contains at least 210 mM and/or at most 845 mM of sodium sulphate.
  • the plating temperature is at least 40 °C, preferably at least 50 °C, more preferably at least 55 °C.
  • the line speed of the plating line is at least 100 m/min, more prefebrably at least 200 m/min.
  • the coated blackplate is further coated on one or both sides by a film lamination step or a direct extrusion step, with an organic coating consisting of a thermoplastic single layer, or a thermoplastic multi-layer polymer, preferably wherein the thermoplastic polymer coating is a polymer coating system comprising one or more layers comprising thermoplastic resins such as polyesters or polyolefins, acrylic resins, polyamides, polyvinyl chloride, fluorocarbon resins, polycarbonates, styrene type resins, ABS resins, chlorinated polyethers, ionomers, urethane resins and functionalised polymers; and/or copolymers thereof; and or blends thereof.
  • thermoplastic resins such as polyesters or polyolefins, acrylic resins, polyamides, polyvinyl chloride, fluorocarbon resins, polycarbonates, styrene type resins, ABS resins, chlorinated polyethers, ionomers, urethane resins and functionalised
  • the blackplate provided with a chromium metal - chromium oxide coating obtained by the process according to the invention has a shiny coating is shiny and shows no stripy appearance.
  • the invention is also embodied in the use of the chromium metal - chromium oxide coated blackplate obtainable by the process according to the invention in a process to produce containers for packaging purposes.
  • an organic coating is provided on one or both sides of the chromium metal - chromium oxide coated blackplate substrate. It was found that organic coatings could be readily applied on to the chromium-chromium oxide coating, which itself acts a passivation layer to protect the electrically conductive substrate. The chromium-chromium oxide coating also exhibited good adhesion the subsequently applied organic coating.
  • the organic coating may be provided as a lacquer or as a thermoplastic polymer coating.
  • thermoplastic polymer coating is a polymer coating system that comprises one or more layers of thermoplastic resins such as polyesters or polyolefins, but can also include acrylic resins, polyamides, polyvinyl chloride, fluorocarbon resins, polycarbonates, styrene type resins, ABS resins, chlorinated polyethers, ionomers, urethane resins and functionalised polymers.
  • thermoplastic resins such as polyesters or polyolefins
  • acrylic resins such as polyesters or polyolefins
  • fluorocarbon resins such as polyamides, polyvinyl chloride, fluorocarbon resins, polycarbonates, styrene type resins, ABS resins, chlorinated polyethers, ionomers, urethane resins and functionalised polymers.
  • Polyester is a polymer composed of dicarboxylic acid and glycol.
  • suitable dicarboxylic acids include therephthalic acid, isophthalic acid, naphthalene dicarboxylic acid and cyclohexane dicarboxylic acid.
  • suitable glycols include ethylene glycol, propane diol, butane diol, hexane diol, cyclohexane diol, cyclohexane dimethanol, neopentyl glycol etc. More than two kinds of dicarboxylic acid or glycol may be used together.
  • Polyolefins include for example polymers or copolymers of ethylene, propylene, 1- butene, 1-pentene, 1-hexene or 1-octene.
  • Acrylic resins include for example polymers or copolymers of acrylic acid, methacrylic acid, acrylic acid ester, methacrylic acid ester or acrylamide.
  • Polyamide resins include for example so-called Nylon 6, Nylon 66, Nylon 46, Nylon 610 and Nylon 11.
  • Polyvinyl chloride includes homopolymers and copolymers, for example with ethylene or vinyl acetate.
  • Fluorocarbon resins include for example tetrafluorinated polyethylene, trifluorinated monochlorinated polyethylene, hexafluorinated ethylene-propylene resin, polyvinyl fluoride and polyvinylidene fluoride.
  • Functionalised polymers for instance by maleic anhydride grafting include for example modified polyethylenes, modified polypropylenes, modified ethylene acrylate copolymers and modified ethylene vinyl acetates.
  • thermoplastic polymer coating systems have shown to provide excellent performance in can-making and use of the can, such as shelf-life.
  • lacquers can be applied, for food and non-food applications. All show excellent adhesion, when enough chromium oxide is present on the surface of the coated blackplate according to the invention. Chromium oxide levels of 4 mg/m 2 or more give satisfactory lacquer adhesion.
  • the application process of the thermoplastic polymer coating is preferably performed by laminating a polymer film onto the coated blackplate by means of extrusion coating and lamination, wherein a polymer resin is melted and formed into thin hot film, which is coated onto the moving substrate.
  • the coated substrate then usually passes between a set of counter-rotating rolls, which press the coating onto the substrate to ensure complete contact and adhesion.
  • film lamination where a film of the polymer is supplied and coated onto a heated substrate and pressed onto the substrate by and between a set of counter-rotating rolls to ensure complete contact and adhesion.
  • An electrolyte was prepared having a sodium formate concentration of 20 g/l (294 mM), a sodium sulphate concentration of 80 g/l (563 mM) and a pH of 2.6, 2.15 and 2.0, and a chromium concentration of 10 g/l (192 mM).
  • the formate/Cr 3+ ratio 1.53.
  • the appearance is not stripy, with the better appearance being obtained with the lower pH-values.
  • Stripe free and shiny surfaces were obtained at line speeds of 100 and 200 m/min or higher.
  • Figure 5A shows the total amount of chromium deposited at different anode currents for two line speeds.
  • Figure 5 only shows part of regme III for the line speed of 200 m/min. Higher currents are required to move to regime III.
  • the amount of chromium oxide can be quantified according to EN 10202:2001, E 2.5.2. First the total amount of chromium is measured by XRF. Then the sample is placed in a 30wt% NaOH solution kept at 90 °C for 10 minutes. This dissolves the chromium present as chromium oxide or hydroxide and the chromium carbide and chromium metal stays behind. After thoroughly rinsing again the total amount of chromium is determined again with XRF.
  • the difference between the 2 measurements is amount of chromium present as chromium oxide or hydroxide on the surface according to the following formula (the factor 1.46 comes from the ratio of the molar weight of Cr 2 C> 3 and Cr ((2x52+3xl6)/(2x52):
  • CC0CC delivers a combination of 92.5 mg/m 2 total Cr (i.e. metal, oxide and carbide) and of 10.6 mg/m 2 Cr-oxide.
  • the currentless episode is apparently beneficial for the formation of Cr-oxide and Cr-metal.
  • another combination can be chosen.
  • the XOXOX combination results in much lower amount of oxide (3.2) and about the same total Cr (90.5).
  • Experiment 2 and 3 relate to the deposition of chromium metal - chromium oxide coating with an enlarged amount of oxide (regime Illb). So in order to produce a coated blackplate this needs to be combined with the deposition of a chromium metal - chromium oxide coating in regime II.
  • Figure 5C shows a part of Figure 5B with regime II represented as a straight dashed line.
  • the thickness of the first chromium metal - chromium oxide coating layer can be controlled.
  • a subsequent deposition of the second chromium metal - chromium oxide coating layer can then be achieved by increasing the current into the regime III region, i.e. 450 or higher as demonstrated in Figure 5B.
  • the current density at which the desired chromium coating weight and composition are obtained depends on the electrolyte composition, pH, temperature and mass transfer rate (strip speed in case of a strip plating line).
  • the optimal current density is not a discrete value, but a range of values restricted by a lower and an upper limit. This current density range is called the 'plating window'. Within the plating window, the coating properties fall within certain specifications. From an operational perspective, a large plating window is desired, because this simplifies process control.
  • titanium anodes comprising a catalytic coating or mixed metal oxide of iridium oxide and tantalum oxide are chosen.
  • the substrate was a 0.183 mm thick cold rolled blackplate material and the dimensions of the cylinder were 113.3 mm x ⁇ 73 mm. The cylinders were cleaned and activated under the following conditions prior to plating.
  • Figure 1 Schematic process route of starting material for the coating process according to the invention.
  • Figure 3 Schematic principle of the chromium deposition mechanism
  • Figure 4A Chromium coating weight as a function of current density showing the 3 different deposition regimes.
  • Figure 4B as Figure 4A with explanation of regime Ilia and Illb.
  • Figure 5A I-Cr curve for plating line speed of 100 and 200 m/min.
  • Figure 5B I-Cr curve for plating line speed of 150 m/min at 40°C, 192 mM Cr(III), 288 mM HCOONa (20 g/l), 80 g/l sodium sulphate.
  • Figure 5C as Figure 5B for regime II and linear interpolation.
  • Figure 8 Schematic presentation of 5 cell plating line with 10 anode pairs and some possible switching options. II is current in regime II, III is current in regime III (preferably Illb) and 0 is no current. The table shows which of the 10 anode pairs is operated in which regime.
  • Figure 9 Schematic presentation of 1 cell plating line with 7 anode pairs and some possible switching options. II is current in regime II, III is current in regime III (preferably Illb) and 0 is no current. The table shows which of the 7 anode pairs is operated in which regime.

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  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Abstract

L'invention concerne un procédé pour l'électrodéposition d'un fer noir non revêtu avec une couche de placage et une amélioration de celui-ci. L'invention porte également sur un procédé dans lequel le fer noir revêtu est en outre revêtu sur un côté ou sur les deux côtés par une étape de stratification de film ou une étape d'extrusion directe, et sur l'utilisation dudit fer noir revêtu dans un processus pour produire des récipients à des fins d'emballage.
PCT/EP2018/085335 2017-12-22 2018-12-17 Procédé pour fabriquer un fer noir revêtu de chrome-oxyde de chrome WO2019121582A1 (fr)

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Application Number Priority Date Filing Date Title
EP18829799.8A EP3728701A1 (fr) 2017-12-22 2018-12-17 Procédé pour fabriquer un fer noir revêtu de chrome-oxyde de chrome

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EP17210531 2017-12-22
EP17210531.4 2017-12-22

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DE102018132074A1 (de) * 2018-12-13 2020-06-18 thysenkrupp AG Verfahren zur Herstellung eines mit einer Beschichtung aus Chrom und Chromoxid beschichteten Metallbands auf Basis einer Elektrolytlösung mit einer dreiwertigen Chromverbindung

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US20110274922A1 (en) * 2008-11-14 2011-11-10 Jfe Steel Corporation Colored and laminated metal plate for container
WO2014202316A1 (fr) 2013-06-20 2014-12-24 Tata Steel Ijmuiden B.V. Procédé permettant de fabriquer des substrats recouverts de chrome-d'oxyde de chrome
WO2015177314A1 (fr) 2014-05-21 2015-11-26 Tata Steel Ijmuiden B.V. Procédé permettant de plaquer une bande métallique mobile, et bande métallique revêtue ainsi produite
WO2015177215A1 (fr) 2014-05-20 2015-11-26 Crag - Centre De Recerca En Agrigenòmica Csic Irta Uab Ub Procédé pour améliorer l'efficacité de l'utilisation de l'eau et la tolérance à la sécheresse dans des plantes

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US4473448A (en) * 1981-02-09 1984-09-25 W. Canning Materials Limited Electrodeposition of chromium
US4472250A (en) * 1981-11-18 1984-09-18 International Business Machines Corporation Bath and process for the electrodeposition of chromium
US6004448A (en) * 1995-06-06 1999-12-21 Atotech Usa, Inc. Deposition of chromium oxides from a trivalent chromium solution containing a complexing agent for a buffer
US20110274922A1 (en) * 2008-11-14 2011-11-10 Jfe Steel Corporation Colored and laminated metal plate for container
WO2014202316A1 (fr) 2013-06-20 2014-12-24 Tata Steel Ijmuiden B.V. Procédé permettant de fabriquer des substrats recouverts de chrome-d'oxyde de chrome
WO2015177215A1 (fr) 2014-05-20 2015-11-26 Crag - Centre De Recerca En Agrigenòmica Csic Irta Uab Ub Procédé pour améliorer l'efficacité de l'utilisation de l'eau et la tolérance à la sécheresse dans des plantes
WO2015177314A1 (fr) 2014-05-21 2015-11-26 Tata Steel Ijmuiden B.V. Procédé permettant de plaquer une bande métallique mobile, et bande métallique revêtue ainsi produite

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