EP2180088B2 - Procédé de dépôt galvanique de couches en chrome dur - Google Patents
Procédé de dépôt galvanique de couches en chrome dur Download PDFInfo
- Publication number
- EP2180088B2 EP2180088B2 EP08018462.5A EP08018462A EP2180088B2 EP 2180088 B2 EP2180088 B2 EP 2180088B2 EP 08018462 A EP08018462 A EP 08018462A EP 2180088 B2 EP2180088 B2 EP 2180088B2
- Authority
- EP
- European Patent Office
- Prior art keywords
- substrate surface
- electrolyte
- chromium
- chromium layer
- layer
- 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.)
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- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 title claims description 83
- 238000000034 method Methods 0.000 title claims description 24
- 238000009713 electroplating Methods 0.000 title 1
- 229910052804 chromium Inorganic materials 0.000 claims description 61
- 239000011651 chromium Substances 0.000 claims description 61
- 239000000758 substrate Substances 0.000 claims description 43
- 239000003792 electrolyte Substances 0.000 claims description 42
- 230000008021 deposition Effects 0.000 claims description 28
- 239000010410 layer Substances 0.000 description 73
- 238000000151 deposition Methods 0.000 description 31
- 238000005260 corrosion Methods 0.000 description 12
- 230000007797 corrosion Effects 0.000 description 11
- 238000000576 coating method Methods 0.000 description 9
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 7
- 238000004070 electrodeposition Methods 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000007935 neutral effect Effects 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- AWJWCTOOIBYHON-UHFFFAOYSA-N furo[3,4-b]pyrazine-5,7-dione Chemical compound C1=CN=C2C(=O)OC(=O)C2=N1 AWJWCTOOIBYHON-UHFFFAOYSA-N 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000008237 rinsing water Substances 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 239000010955 niobium Substances 0.000 description 1
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 229910052715 tantalum Inorganic materials 0.000 description 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002347 wear-protection layer Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/04—Removal of gases or vapours ; Gas or pressure control
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
-
- 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
- C25D5/003—Electroplating using gases, e.g. pressure influence
-
- 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
- C25D5/04—Electroplating with moving electrodes
-
- 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
- C25D5/08—Electroplating with moving electrolyte e.g. jet electroplating
-
- 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
- C25D5/10—Electroplating with more than one layer of the same or of different metals
- C25D5/12—Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or 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
- C25D5/60—Electroplating characterised by the structure or texture of the layers
- C25D5/623—Porosity of the layers
-
- 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
- C25D5/60—Electroplating characterised by the structure or texture of the layers
- C25D5/625—Discontinuous layers, e.g. microcracked layers
-
- 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
- C25D7/10—Bearings
Definitions
- the present invention relates to a method for depositing a hard chromium layer on a substrate surface.
- the present invention relates to a method for depositing hard chromium layers at high deposition rates.
- Hard chrome layers are widely used as coatings of engineering components. For example, it is known to provide valve bodies, liners, brake pistons or axle hubs with hard chrome layers.
- the deposited chromium layer serves on the one hand as a corrosion protection layer for the underlying substrate surface, on the other hand, as a tribological wear protection layer, since the deposited hard chrome layers have a high hardness.
- the substrate surfaces to be coated are brought into contact with an electrolyte having at least the metal (chromium) to be deposited after a suitable pretreatment for the surface, wherein a deposition voltage is applied between the cathodically contacted substrate surface and an anode.
- a deposition voltage is applied between the cathodically contacted substrate surface and an anode.
- the layers thus deposited may have tensile or compressive residual stresses. Compressive stresses can cause the deposited layers to be microcracked, which means that the layers are not continuous, but have a network of microcracks.
- Inherent tensile stresses can lead to deep cracks in the deposited layers into which moisture or aggressive substances migrate and thus can lead to corrosion phenomena of the substrate surface located beneath the chromium layer, as a result of which damage to the chromium layer up to its flaking off can occur.
- the coated substrate surfaces in the prior art are mechanically reworked, for example by grinding or honing, in order to break down the inherent tensile stresses occurring in the layers.
- the processing can also lead to a violation of the deposited chromium layers, which ultimately drastically reduces their property as a corrosion protection layer.
- chromium is itself a chemically relatively non-noble metal
- chromium layers have a corrosion-protective effect due to the formation of a thin oxide layer on the surface and the associated very positive potential.
- Corrosion and tarnish protection with precious metals such as gold, silver or platinum shows comparable corrosion protection properties.
- the crack network occurring in the electrodeposited chromium layers due to residual compressive stresses not only has a negative influence on the anticorrosive property of the deposited layer, but also leads to improved mechanical properties of the so coated running parts, since any lubricants to reduce the tribological resistance between moving components in the Microcracks can store the so have a depot effect for the lubricant.
- This ability of the layers is termed oil carrying capacity and is consistently desired for corresponding mechanical components. This is important, for example, in the case of piston rings to maintain the fire stability.
- GB 1 551 340 A discloses the deposition of a hard chromium layer on a substrate surface at a temperature of 60 ° C and a set current density of 80 A / dm 2 in a vacuum chamber through which a chromium deposition electrolyte flows.
- US 2,706,175 A discloses a device for internal coating of hollow cylinders, wherein a chromium layer is deposited under negative pressure.
- EP 1 191 129 A discloses a method for depositing a hard chromium layer under negative pressure, wherein the electrolyte and substrate are moved relative to each other at a relative speed of 0.4 m / s.
- US 2001/054557 A1 discloses a method for the electrodeposition of hard chromium layers, in which the chromium layer is also under reduced pressure at a Current density of 30 to 40 A / dm 2 and a pulse frequency of 5 to 700 Hz is deposited.
- EP 0 024 946 A discloses a process for the deposition of hard chromium layers in vacuum at a current density in the range of 200 A / dm 2 and the generation of a relative movement between the electrolyte and the substrate to be coated.
- US 5,277,785 discloses a method and apparatus for depositing hard chromium layers by brush deposition.
- the pressure difference to be set is in a range from 20 mbar to 200 mbar.
- a second hard chromium layer is deposited on a first deposited hard chrome layer, a pulse current being applied between the substrate surface and counterelectrode for depositing the first hard chrome layer and a direct current being applied to deposit the second hard chrome layer on the first hard chrome layer.
- a first hard chrome layer is deposited, which has no residual stresses due to the applied pulse current and is free of microcracks.
- a direct current between the substrate surface to be coated and the counter electrode is deposited on the already deposited intrinsic and crack-free first hard chrome layer, a second hard chrome layer, which has tensile residual stress and the mechanically desired microcracking.
- the layer composite obtained in this way exhibits excellent corrosion resistance and moreover has excellent mechanical properties as running or sliding surfaces due to the microcracks occurring in the upper chromium layer.
- the pulse current is applied at a pulse frequency of 5 Hz to 5000 Hz, preferably 50 Hz to 1000 Hz.
- a current density between 25 A / dm 2 and 1000 A / dm 2 , preferably 50 A / dm 2 to 500 A / dm 2 is set.
- a direct current with a current density in the range between 25 A / dm 2 and 1000 A / dm 2 , also with a preferred range between 50 A / dm 2 and 500 A / dm 2 is set.
- the substrate surface to be coated can with the chromium-containing electrolyte.
- the electrolyte may have a pH in the range ⁇ pH 3, preferably ⁇ pH 1.
- the chromium-containing electrolyte has a conductivity K of from 200 mS / cm to 550 mS / cm (at 20 ° C.).
- the process can be carried out with only one electrolyte in a single coating cell.
- the relative speed here is in a range between 0.1 m / s and 5.0 m / s.
- the substrate surfaces can be moved or the electrolyte can be conveyed accordingly.
- agitators or pumps are suitable for conveying the electrolyte.
- the substrate surface to be coated is contacted with the electrolyte in a cell in which the chromium-containing electrolyte flows from below and can flow off via an overflow, with a sufficient flow rate is adjusted to the peeling to support the resulting hydrogen bubbles.
- a coating reactor is particularly suitable, which is cylindrical and is equipped with a cylindrical inner anode made of platinized metal such as platinum-plated titanium, niobium or tantalum. At the top and bottom of the coating reactor can be recordings for the component to be chromed.
- a coating reactor designed in this way is particularly suitable for coating cylindrical components. At least one of the two receptacles serves to supply power to the component to be coated and is accordingly designed as an electrical contact.
- an electrolyte is sucked from a reservoir through the reactor to the upper part of the reactor by means of a suitable pump and conveyed by this back into the reservoir.
- the electrolyte can be degassed by means of suitable facilities.
- the gas mixture to be separated off is discharged to the outside via a mist eliminator.
- a separate degassing container may be provided.
- means for controlling the temperature of the electrolyte ie heaters and / or cooling can be provided.
- the reservoir can be connected via metering with other reservoirs, which receive compositions for supplementing the electrolyte contained in the reservoir, if a re-dosing of the electrolyte is necessary.
- electrolyte can be passed through an evaporator unit, wherein the electrolyte is deprived of water and this is cooled simultaneously.
- such a reactor designed according to the invention is equipped with at least one movable end face, which facilitates the supply and removal of the component to be coated.
- conventional handling systems and seals may be provided to automate the process.
- the coated component can be rinsed in the reactor with rinsing water or steam or at least pre-rinsed.
- the electrolyte supply to the reactor can be interrupted and replaced by rinsing water or steam.
- the final rinse can take place in a second reactor, which is essentially identical in construction to the first reactor, but has no anode and power supply.
- a work piece to be chromium plated (CK 45 steel piston rods) was contacted in a reactor constructed in accordance with the invention with an electrolyte for depositing a hard chromium layer comprising 370 g / l chromic acid and 5.3 g / l sulfuric acid, the electrolyte from below in the corresponding reactor flowed in and was discharged via an upper course at the top of the reactor.
- the relative velocity set here between the substrate surface of the workpiece to be coated and the electrolyte was 4 m / s.
- the electrolyte had a temperature of 70 ° C.
- a pressure of 50 mbar was set within the reactor.
- a hard chrome layer was subsequently deposited by setting a current density of 235 A / dm 2 within 300 seconds. Subsequently, the substrate was rinsed.
- the chromium layer obtained had a layer thickness of 11 microns, showed about 40 cracks / cm and had a corrosion resistance in the neutral salt spray test of less than 100 h.
- a workpiece to be chrome plated was contacted with an electrolyte as in Example 1 in a reactor constructed according to the invention, which had 370 g / l chromic acid, 5.3 g / l sulfuric acid and 6 g / l methanesulfonic acid.
- the deposition conditions corresponded to Example 1.
- a shiny chromium layer was obtained with a layer thickness of 11 microns, which showed about 250 cracks / cm and a corrosion resistance in the neutral salt spray test less than 100 h.
- a workpiece to be chromium plated was contacted with the electrolyte according to Example 2 under the conditions mentioned in Example 2, wherein a pulse current with a current density during the pulse of 235 A / dm 2 , a frequency of 1000 Hz and a duty cycle of 50% for 400 seconds was created.
- a bright, crack-free chromium layer with a layer thickness of 11 ⁇ m was obtained which showed 0 cracks / cm and a corrosion resistance in the neutral salt spray test of greater than 500 h.
- a work piece to be chrome plated was coated under the deposition conditions of Example 1 except that first a pulse current with a current density of 235 A / dm 2 was applied during the pulse, a frequency of 1000 Hz and a duty cycle of 50% for 400 seconds and then in the same electrolyte under otherwise identical conditions, a direct current with a current density of 235 A / dm 2 was applied for 100 seconds.
- the obtained shiny chromium layer showed a layer thickness of 17 ⁇ m and had about 25 cracks / cm, the layer having a corrosion resistance in the neutral salt spray test of greater than 500 h.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
Claims (4)
- Procédé de dépôt galvanique d'une couche en chrome dur sur la surface d'un substrat, comportant les étapes de procédé :- mise en contact de la surface du substrat qui doit être revêtue avec un électrolyte chromifère adapté pour le dépôt galvanique;- application d'une tension entre la surface de substrat qui doit être revêtue et une contre-électrode, pour le dépôt galvanique d'une couche en chrome dur sur la surface du substrat,le dépôt s'effectuant dans un conteneur sensiblement étanche au gaz par rapport à l'environnement, au moins pendant l'application de la tension, une dépression étant établie dans le conteneur sensiblement étanche au gaz par rapport à l'environnement et la surface du substrat et l'électrolyte chromifère étant déplacés l'un vers l'autre à une vitesse relative de > 1 m/s à 5 m/s, caractérisé en ce que sur une première couche de chrome dur déposé, on dépose une deuxième couche de chrome dur, un courant d'impulsion étant appliqué entre la surface du substrat et la contre-électrode pour le dépôt de la première couche de chrome dur, et un courant continu étant appliqué pour le dépôt de la deuxième couche de chrome dur sur la première couche de chrome dur, une pression différentielle comprise entre 20 mbar et 200 mbar par rapport à la pression ambiante étant établie, une tension d'impulsion d'une fréquence de 5 Hz à 5000 Hz, de préférence comprise entre 50 Hz et 1000 Hz étant appliquée pour le dépôt de la première couche de chrome dur, et un courant de densité comprise entre 25 A/dm2 et 1000 A/dm2, de préférence comprise entre 50 A/dm2 et 500 A/dm2 étant établi pour le dépôt de la première couche de chrome dur, et l'électrolyte chromifère comporte une conductivité K de 200 mS/cm à 550 mS/cm à 20 °C.
- Procédé selon l'une quelconque des revendications précédentes, la surface du substrat qui doit être revêtue étant mise en contact avec l'électrolyte chromifère à une température comprise entre 30°C et 85°C.
- Procédé selon l'une quelconque des revendications précédentes, une valeur pH de l'ordre de < pH 3, de préférence de < pH 1 étant établie dans l'électrolyte.
- Procédé selon l'une quelconque des revendications précédentes, la surface du substrat qui doit être revêtue étant mise en contact avec l'électrolyte dans une cellule dans laquelle l'électrolyte chromifère afflue par le dessous et s'écoule via un trop-plein.
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES08018462T ES2363566T5 (es) | 2008-10-22 | 2008-10-22 | Procedimiento para la deposición galvánica de capas de cromo duro |
PL08018462T PL2180088T5 (pl) | 2008-10-22 | 2008-10-22 | Sposób galwanicznego nakładania warstwy twardego chromu |
EP08018462.5A EP2180088B2 (fr) | 2008-10-22 | 2008-10-22 | Procédé de dépôt galvanique de couches en chrome dur |
US13/125,622 US20110198226A1 (en) | 2008-10-22 | 2009-10-22 | Method for deposition of hard chrome layers |
BRPI0920600-0A BRPI0920600B1 (pt) | 2008-10-22 | 2009-10-22 | Método para deposição galvânica de uma camada de cromo resistente sobre uma superfície de substrato |
KR1020117011605A KR101658254B1 (ko) | 2008-10-22 | 2009-10-22 | 경질 크롬 층의 갈바니 침착 방법 |
PCT/US2009/061683 WO2010048404A1 (fr) | 2008-10-22 | 2009-10-22 | Procédé de dépôt galvanique de couches de chrome dur |
JP2011533333A JP5739341B2 (ja) | 2008-10-22 | 2009-10-22 | 基板表面に硬質クロム層を沈着する方法及び該硬質クロム層を表面に有してなる基板 |
CN200980151479.6A CN102257184B (zh) | 2008-10-22 | 2009-10-22 | 硬铬层的电沉积方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08018462.5A EP2180088B2 (fr) | 2008-10-22 | 2008-10-22 | Procédé de dépôt galvanique de couches en chrome dur |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2180088A1 EP2180088A1 (fr) | 2010-04-28 |
EP2180088B1 EP2180088B1 (fr) | 2011-05-11 |
EP2180088B2 true EP2180088B2 (fr) | 2019-06-12 |
Family
ID=40427109
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08018462.5A Active EP2180088B2 (fr) | 2008-10-22 | 2008-10-22 | Procédé de dépôt galvanique de couches en chrome dur |
Country Status (9)
Country | Link |
---|---|
US (1) | US20110198226A1 (fr) |
EP (1) | EP2180088B2 (fr) |
JP (1) | JP5739341B2 (fr) |
KR (1) | KR101658254B1 (fr) |
CN (1) | CN102257184B (fr) |
BR (1) | BRPI0920600B1 (fr) |
ES (1) | ES2363566T5 (fr) |
PL (1) | PL2180088T5 (fr) |
WO (1) | WO2010048404A1 (fr) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ES2766775T3 (es) * | 2013-09-05 | 2020-06-15 | Macdermid Enthone Inc | Composición acuosa de electrolito que tiene una emisión aérea reducida |
ES2726301T3 (es) * | 2014-12-19 | 2019-10-03 | Weber Hydraulik Gmbh | Procedimiento para rotular y/o marcar redondos ópticamente |
US11566679B2 (en) * | 2020-11-03 | 2023-01-31 | DRiV Automotive Inc. | Bumper cap for damper |
CN114703516A (zh) * | 2021-12-14 | 2022-07-05 | 西安昆仑工业(集团)有限责任公司 | 一种火炮身管快速镀铬工艺方法 |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19953318A1 (de) † | 1998-11-06 | 2000-06-21 | Tokico Ltd | Chromplattierte Teile und Chromplattierungsverfahren |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE494578A (fr) | 1949-03-18 | |||
FI53841C (fi) | 1975-05-07 | 1978-08-10 | Teuvo Tapio Korpi | Elektrolytisk ytbelaeggningsanordning |
FR2462490A1 (fr) * | 1979-08-03 | 1981-02-13 | Centre Techn Ind Mecanique | Dispositif de revetement electrolytique |
US4261086A (en) | 1979-09-04 | 1981-04-14 | Ford Motor Company | Method for manufacturing variable capacitance pressure transducers |
JPS62263991A (ja) * | 1986-05-07 | 1987-11-16 | Adachi Shin Sangyo Kk | 鍍金物製造法 |
JPH02217429A (ja) * | 1989-02-17 | 1990-08-30 | Fujitsu Ltd | メッキ方法および装置 |
US5277785A (en) | 1992-07-16 | 1994-01-11 | Anglen Erik S Van | Method and apparatus for depositing hard chrome coatings by brush plating |
US20010054557A1 (en) | 1997-06-09 | 2001-12-27 | E. Jennings Taylor | Electroplating of metals using pulsed reverse current for control of hydrogen evolution |
USRE40386E1 (en) * | 1998-11-06 | 2008-06-17 | Hitachi Ltd. | Chrome plated parts and chrome plating method |
JP2002047595A (ja) * | 2000-07-31 | 2002-02-15 | Tokico Ltd | クロムめっき方法およびクロムめっき装置 |
JP3423702B2 (ja) * | 2000-08-29 | 2003-07-07 | 創輝株式会社 | 金属めっき方法 |
SG130126A1 (en) * | 2005-08-08 | 2007-03-20 | Nanofilm Technologies Int | Metal coatings |
-
2008
- 2008-10-22 PL PL08018462T patent/PL2180088T5/pl unknown
- 2008-10-22 EP EP08018462.5A patent/EP2180088B2/fr active Active
- 2008-10-22 ES ES08018462T patent/ES2363566T5/es active Active
-
2009
- 2009-10-22 BR BRPI0920600-0A patent/BRPI0920600B1/pt active IP Right Grant
- 2009-10-22 WO PCT/US2009/061683 patent/WO2010048404A1/fr active Application Filing
- 2009-10-22 JP JP2011533333A patent/JP5739341B2/ja active Active
- 2009-10-22 US US13/125,622 patent/US20110198226A1/en not_active Abandoned
- 2009-10-22 CN CN200980151479.6A patent/CN102257184B/zh active Active
- 2009-10-22 KR KR1020117011605A patent/KR101658254B1/ko active IP Right Grant
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19953318A1 (de) † | 1998-11-06 | 2000-06-21 | Tokico Ltd | Chromplattierte Teile und Chromplattierungsverfahren |
Non-Patent Citations (1)
Title |
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"Modern Electroplating", part 7 2000, JOHN WILEY &SONS, ISBN: 0-471-16824-6, article MANDICH, N.V. ET AL: "Electrodeposition of Chromium", pages: 289 - 292 † |
Also Published As
Publication number | Publication date |
---|---|
US20110198226A1 (en) | 2011-08-18 |
BRPI0920600B1 (pt) | 2019-05-28 |
KR101658254B1 (ko) | 2016-09-20 |
WO2010048404A1 (fr) | 2010-04-29 |
PL2180088T3 (pl) | 2011-09-30 |
JP2012506496A (ja) | 2012-03-15 |
KR20110075028A (ko) | 2011-07-05 |
CN102257184B (zh) | 2014-01-15 |
EP2180088A1 (fr) | 2010-04-28 |
ES2363566T5 (es) | 2020-04-16 |
PL2180088T5 (pl) | 2020-11-16 |
EP2180088B1 (fr) | 2011-05-11 |
JP5739341B2 (ja) | 2015-06-24 |
CN102257184A (zh) | 2011-11-23 |
ES2363566T3 (es) | 2011-08-09 |
BRPI0920600A2 (pt) | 2015-12-22 |
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