US20120024714A1 - Trivalent chromium plating solution and plating method using the same - Google Patents
Trivalent chromium plating solution and plating method using the same Download PDFInfo
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- US20120024714A1 US20120024714A1 US13/188,515 US201113188515A US2012024714A1 US 20120024714 A1 US20120024714 A1 US 20120024714A1 US 201113188515 A US201113188515 A US 201113188515A US 2012024714 A1 US2012024714 A1 US 2012024714A1
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- plating solution
- plating
- trivalent chromium
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- 238000007747 plating Methods 0.000 title claims abstract description 142
- 239000011651 chromium Substances 0.000 title claims abstract description 56
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 title claims abstract description 54
- 229910052804 chromium Inorganic materials 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims description 22
- 150000001845 chromium compounds Chemical class 0.000 claims abstract description 21
- 150000001875 compounds Chemical class 0.000 claims abstract description 14
- 239000003795 chemical substances by application Substances 0.000 claims description 44
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 claims description 35
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 12
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical group NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 12
- 239000000080 wetting agent Substances 0.000 claims description 12
- 239000008139 complexing agent Substances 0.000 claims description 11
- 230000003213 activating effect Effects 0.000 claims description 10
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 10
- 229910000329 aluminium sulfate Inorganic materials 0.000 claims description 8
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 8
- 235000011128 aluminium sulphate Nutrition 0.000 claims description 8
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims description 7
- 239000004327 boric acid Substances 0.000 claims description 7
- 229910001430 chromium ion Inorganic materials 0.000 claims description 7
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical group [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 6
- 239000004202 carbamide Substances 0.000 claims description 6
- 235000013877 carbamide Nutrition 0.000 claims description 6
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 6
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 6
- 235000011152 sodium sulphate Nutrition 0.000 claims description 6
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 5
- 235000019253 formic acid Nutrition 0.000 claims description 5
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 239000000853 adhesive Substances 0.000 claims description 4
- 230000001070 adhesive effect Effects 0.000 claims description 4
- 238000006116 polymerization reaction Methods 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical group [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 3
- 230000000996 additive effect Effects 0.000 claims description 3
- -1 alkali metal formate Chemical class 0.000 claims description 3
- 235000019333 sodium laurylsulphate Nutrition 0.000 claims description 3
- 230000000087 stabilizing effect Effects 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 2
- VZTDIZULWFCMLS-UHFFFAOYSA-N ammonium formate Chemical compound [NH4+].[O-]C=O VZTDIZULWFCMLS-UHFFFAOYSA-N 0.000 claims description 2
- HTXDPTMKBJXEOW-UHFFFAOYSA-N dioxoiridium Chemical compound O=[Ir]=O HTXDPTMKBJXEOW-UHFFFAOYSA-N 0.000 claims description 2
- UBXWAYGQRZFPGU-UHFFFAOYSA-N manganese(2+) oxygen(2-) titanium(4+) Chemical compound [O--].[O--].[Ti+4].[Mn++] UBXWAYGQRZFPGU-UHFFFAOYSA-N 0.000 claims description 2
- WOCIAKWEIIZHES-UHFFFAOYSA-N ruthenium(iv) oxide Chemical compound O=[Ru]=O WOCIAKWEIIZHES-UHFFFAOYSA-N 0.000 claims description 2
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 12
- 230000008569 process Effects 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000012153 distilled water Substances 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 6
- KRVSOGSZCMJSLX-UHFFFAOYSA-L chromic acid Substances O[Cr](O)(=O)=O KRVSOGSZCMJSLX-UHFFFAOYSA-L 0.000 description 5
- 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 5
- 239000007787 solid Substances 0.000 description 5
- 238000009713 electroplating Methods 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- 239000000047 product Substances 0.000 description 3
- GRWVQDDAKZFPFI-UHFFFAOYSA-H chromium(III) sulfate Chemical compound [Cr+3].[Cr+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRWVQDDAKZFPFI-UHFFFAOYSA-H 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000010338 boric acid Nutrition 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000011889 copper foil Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000002498 deadly effect Effects 0.000 description 1
- 238000004070 electrodeposition Methods 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000007733 ion plating Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005121 nitriding Methods 0.000 description 1
- 238000007750 plasma spraying Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000002310 reflectometry Methods 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- 125000001273 sulfonato group Chemical group [O-]S(*)(=O)=O 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Images
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
Definitions
- the present invention relates to a trivalent chromium plating solution and a plating method using the same, and more particularly, to a hard trivalent chromium plating solution having improved covering power.
- Chrome plating is the most common process among various plating processes and is a final treatment step. Chrome plating may be classified into decorative plating for obtaining a beautifully glossy metal surface and hard plating for increasing wear resistance.
- the plating thickness typically ranges from 0.2 to 0.5 ⁇ m.
- Decorative plating is usually used to plate brass surfaces of tableware and other disposable products.
- the plating thickness may range from approximately 5 to several tens of ⁇ m although it varies according to the required wear life.
- Hard plating is used to prevent a portion of a camera lens to which a screw is tightened, a precision machine, an inner surface of a mold, a surface of a printing plate, etc. from wearing out.
- electroplating is typically performed using a solution of chromic acid (CrO 3 ) mixed with sulfuric acid (H 2 SO 4 ).
- CrO 3 chromic acid
- H 2 SO 4 sulfuric acid
- an element that is not eroded by H 2 SO 4 such as lead, is used instead of chromium metal.
- Electrodeposition is continuously performed while CrO 3 supplement a reduction of chromium in the solution.
- the concentration of CrO 3 in a plating solution used for chrome plating may be high or low, and various forms of coatings can be obtained depending on the temperature of the solution and current density, that is, plating conditions.
- Advantages of hexavalent chromium plating include excellent reflectivity, color and corrosion resistance as well as high current efficiency.
- hexavalent chromium plating produces CrO 3 gas that is fatal to the human body during the plating process.
- hexavalent chromium ions introduced into underground water or rivers may cause deadly environmental contamination. Therefore, hexavalent chromium must be reduced to trivalent chromium.
- hexavalent chromium is classified as a carcinogen by the International Agency of Research on Cancer (IARC). Since the use of hexavalent chromium is expected to be prohibited, alternatives to hexavalent chromium are required. Accordingly, a lot of research is being actively conducted worldwide to develop alternatives to hexavalent chromium.
- IARC International Agency of Research on Cancer
- Examples of alternatives to hexavalent chromium plating include ion-nitriding, plasma spraying, and ion plating. However, these alternatives require 5 to 10 times the cost of hexavalent chromium plating and cannot be applied to large-sized products.
- chrome plating using trivalent chromium is being recognized as the most efficient alternative.
- a conventional trivalent chromium plating solution does not have superior covering power. Thus, it is difficult to apply electroplating on surfaces of machine parts or products having complicated shapes.
- aspects of the present invention provide a trivalent chromium plating solution having superior covering power.
- a trivalent chromium plating solution comprising a trivalent chromium compound including a compound of formula (1) below;
- a plating method comprising preparing a trivalent chromium plating solution in a plating bath, immersing an object to be plated in the trivalent chromium plating solution, and applying a negative potential to the object to be plated and applying a positive potential to an insoluble anode after installing the insoluble anode in the plating bath, wherein the trivalent chromium plating solution comprises a trivalent chromium compound comprising a compound of formula (1) below, a complexing agent suppressing a polymerization reaction of the trivalent chromium compound in the plating solution, a conductivity agent increasing electrical conductivity of trivalent chromium ions, a buffer agent stabilizing a hydrogen ion index of the plating solution, a plating activating additive increasing adhesive power and capability of forming a plated layer, a wetting agent removing a pitting phenomenon which occurs on a plated surface, and a hydrogen ion index adjusting agent adjusting the hydrogen
- FIG. 1 is a process flowchart illustrating a method of preparing a trivalent chromium solution according to the present invention.
- FIG. 2 is a flowchart illustrating a plating process using a trivalent chromium plating solution according to the present invention.
- a trivalent chromium plating solution according to the present invention may include a trivalent chromium compound which provides trivalent chromium ions, a complexing agent which suppresses a polymerization reaction of the trivalent chromium compound in the plating solution, a conductivity agent which increases electrical conductivity of the trivalent chromium ions, a buffer agent which stabilizes a hydrogen ion index of the plating solution, a plating activating agent which increases adhesive power and capability of forming a plated layer, a wetting agent which removes a pitting phenomenon that occurs on a plated surface, and a hydrogen ion index adjusting agent which adjusts the hydrogen ion index of the plating solution.
- the trivalent chromium compound includes a compound of formula (1) below.
- the trivalent chromium compound may be added to the trivalent chromium plating solution in an amount of 0.4 mol/L to 1.3 mol/L, particularly, 0.8 mol/L to 1 mol/L. Trivalent chromium contained in the trivalent chromium compound forms a chromium film.
- the complexing agent may prevent the trivalent chromium ions contained in the trivalent chromium compound from being polymerized in the plating solution.
- the complexing agent may be, for example, formic acid, alkali metal formate, or ammonium formate, but is not limited thereto.
- the complexing agent may be added to the trivalent chromium plating agent in an amount of 0.05 to 2 mol/L, particularly, 0.4 to 0.6 mol/L.
- the conductivity agent may facilitate the formation of a chromium film by increasing electrical conductivity when an object to be plated is immersed in the trivalent chromium plating solution so as to be plated.
- the conductivity agent may be, for exampe, sodium sulfate, but is not limited thereto.
- the conductivity agent may be added to the trivalent chromium plating solution in an amount of 0.1 mol/L to 0.8 mol/L, particularly, 0.2 mol/L to 0.4 mol/L.
- the buffer agent enables the hydrogen ion index (pH) of the trivalent chromium plating solution to remain stably within a predetermined range.
- the buffer agent includes boric acid and aluminium sulfate. As the buffer agent, when both boric acid and aluminium sulfate exist in the trivalent chromium plating solution, high-quality plating can be obtained.
- Boric acid may be contained in the trivalent chromium plating solution in an amount of 0.08 to 1 mol/L, particularly, 0.4 to 0.6 mol/L.
- Aluminium sulfate may be contained in the trivalent chromium plating solution in an amount of 0.05 to 0.2 mol/L, particularly, 0.1 to 0.16 mol/L.
- the plating activating agent facilitates plating using low-current, thereby expanding an effective plating current range.
- the plating activating additive may be, for example, carbamide, but is not limited thereto.
- the plating activating agent may be contained in the trivalent chromium plating solution in an amount of 0.1 to 1.2 mol/L, particularly, 0.4 to 0.6 mol/L.
- the wetting agent may remove the pitting phenomenon that occurs on a plated surface.
- the wetting agent may be a surfactant.
- An example of the surfactant is an organic anion-active surfactant containing a sulfonate group, but is not limited thereto.
- An example of the organic anion-active surfactant is sodium lauryl sulfate (C 12 H 25 SO 4 Na).
- the wetting agent may be contained in the trivalent chromium plating solution in an amount of 0.01 to 1 g/L, particularly, 0.05 to 0.1 g/L.
- the hydrogen ion index adjusting agent may adjust the hydrogen ion index of the trivalent chromium plating solution.
- the hydrogen ion index adjusting agent may be, for example, sulfuric acid (H 2 SO 4 ), sodium hydroxide (NaOH), or sodium carbonate (Na 2 CO 3 ), but is not limited thereto.
- the hydrogen ion index adjusting agent may be added to the trivalent chromium plating solution in an amount that allows the hydrogen ion index of the trivalent chromium plating solution to be in a range of, e.g., 1.1 to 3.5, particularly, 1.4 to 1.8.
- FIG. 1 is a process flowchart illustrating a method of preparing a trivalent chromium solution according to the present invention.
- a trivalent chromium compound is added to heated, distilled water and is then stirred (operation S 100 ).
- the temperature of the distilled water may be approximately 70 to 95° C., and the trivalent chromium compound is stirred until it is completely dissolved in the distilled water.
- the solution having the trivalent chromium compound dissolved therein is filtered (operation S 110 ).
- the solution may be filtered using a paper filter, a fiber filter, or other types of filters.
- a buffer agent and a conductivity agent are added and dissolved in the filtered solution (operation S 120 ).
- the temperature of the solution may be 70 to 80° C.
- the added buffer agent and conductivity agent may be solid. The above solid elements should be completely dissolved in the solution.
- a complexing agent is added to the solution in which the buffer agent and the conductivity agent have been dissolved (operation S 130 ).
- the solution having the buffer agent and the conductivity agent dissolved therein is maintained at a temperature of 70 to 80° C., and the complexing agent is slowly added to the solution.
- a plating bath is covered with a covering member, and the solution having the complexing agent added thereto is maintained at 70 to 80° C. for a predetermined period of time, for example, for approximately one hour (operation S 140 ).
- the solution maintained at 70 to 80° C. for the predetermined period of time is cooled (operation S 150 ).
- the solution may be cooled to approximately 40 to 50° C.
- a plating activating agent is added and dissolved in the cooled solution (operation S 160 ).
- the plating activation agent may be solid and is completely dissolved in the solution at a temperature of 40 to 50° C.
- the plating bath is covered with the covering member, and the solution having the plating activating agent dissolved therein is maintained at a temperature of 40 to 50° C. for a predetermined period of time, for example, for approximately one hour (operation S 170 ).
- the solution maintained at 40 to 50° C. for the predetermined period of time is cooled (operation S 180 ).
- the solution may be cooled to room temperature.
- the volume of a plating solution is adjusted by adding distilled water to the cooled solution.
- a hydrogen ion index of the solution is measured, and, if necessary, the hydrogen ion index of the solution is adjusted by adding a hydrogen ion index adjusting agent to the solution (operation S 190 ).
- a wetting agent is added to the solution having the adjusted hydrogen ion index (operation S 200 ).
- the wetting agent may be added in a predetermined concentration to distilled water, and the distilled water having the wetting agent may be added to the solution having the adjusted hydrogen ion index.
- Distilled water is added to the solution having the wetting agent in order to reach the final volume of the plating solution. Then, the hydrogen ion index of the solution is measured, and, if necessary, the hydrogen ion index of the solution is adjusted again by adding the hydrogen ion index adjusting agent (operation S 210 ).
- FIG. 2 is a flowchart illustrating a plating process using a trivalent chromium plating solution according to the present invention.
- a trivalent chromium plating solution according to the present invention is prepared within a plating bath (operation S 300 ). Then, an object to be plated is immersed in the trivalent chromium plating solution (operation S 310 ).
- the insoluble anode may be, for example, a titanium-manganese dioxide anode (TMDA), a dimensionally stable anode (DSA) having iridium oxide (IrO 2 ) or ruthenium oxide (RuO 2 ) formed on a porous titanium plate, or a platinized titanium anode, but is not limited thereto.
- TMDA titanium-manganese dioxide anode
- DSA dimensionally stable anode
- IrO 2 iridium oxide
- RuO 2 ruthenium oxide
- TMDA does not require spatial separation of a cathode and an anode in a plating process and does not release toxic chlorine gas during the plating process.
- TMDA noticeably reduces an electrochemical oxidation reaction from trivalent chromium to hexavalent chromium.
- the current density may be 15 to 30 A/dm 2 , particularly, 10 to 20 A/dm 2 .
- a hydrogen ion index of the plating solution may be maintained at 1.1 to 3.5, particularly, 1.4 to 1.8.
- the plating bath may be maintained at a temperature of 20 to 60° C., particularly, 30 to 40° C.
- a chromium-plated film may have a thickness of several tens of ⁇ m.
- the solution having the compound of formula (1) added thereto was filtered, and 0.15 mol of aluminium sulfate, 0.5 mol of boric acid, and 0.3 mol of sodium sulfate were added to the filtered solution at 70 to 80° C. These added solid elements were completely dissolved.
- 0.5 mol of formic acid was slowly added to the solution which contained aluminium sulfate, boric acid and sodium sulfate and which was maintained at 70 to 80° C.
- a plating bath that contained the solution having formic acid added thereto was covered with a covering member and was maintained at 70 to 80° C. for approximately one hour.
- the solution maintained at 70 to 80° C. for approximately one hour was cooled to 40 to 50° C.
- a plating solution was prepared under the same conditions as Embodiment 1, except that the hydrogen ion index was adjusted to 1.7.
- a plating solution was prepared under the same conditions as Embodiment 1, except that the compound of formula (1) was added in an amount of 0.8 mol.
- a plating solution was prepared under the same conditions as Embodiment 1, except that sodium sulfate was added in an amount of 0.2 mol.
- a plating solution was prepared under the same conditions as Embodiment 1, except that the compound of formula (1) was added in an amount of 0.8 mol and that formic acid was added in an amount of 0.4 mol.
- a plating solution was prepared under the same conditions as Embodiment 1, except that carbamide was added in an amount of 0.4 mol and that the hydrogen ion index was adjusted to 1.4.
- a plating solution was prepared by adding 0.5 mol/L of chromium sulfate instead of the compound of formula (1), 0.18 mol/L of aluminium sulfate, 0.63 mol/L of sodium sulfate, 0.45 mol/L of carbamide and 0.66 mol/L of sodium formate.
- the hydrogen ion index was adjusted to 1.4.
- the minimum current densities of the plating solutions of Embodiments 1 through 6 are far lower than that of the plating solution of Comparative Example 1. Accordingly, the plating solutions of Embodiments 1 through 6 using the trivalent chromium compound of formula (1) have better covering power than the plating solution of Comparative Example 1 using a trivalent chromium compound such as chromium sulfate.
- a trivalent chromium plating solution according to the present invention has superior covering power.
- a compound of formula (1) which can also be used as a tanning agent, can be mass-produced and is inexpensive. Therefore, the trivalent chromium plating solution is the first-ever plating solution that provides the compound of formula (1) as a trivalent chromium compound. Using the compound of formula (1) as a source, an economical trivalent chromium plating solution can be produced.
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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 And Plating Baths Therefor (AREA)
- Electroplating Methods And Accessories (AREA)
Abstract
Provided is hard trivalent chromium plating solution having improved covering power. The trivalent chromium plating solution comprises a trivalent chromium compound comprising a compound of formula (1) below;
wherein Cr2(SO4)n(OH)6-2n (n<3) (1).
Description
- This application claims priority from Korean Patent Application No. 10-2010-0073495 filed on Jul. 29, 2010 in the Korean Intellectual Property Office, the disclosure of which is incorporated herein by reference in its entirety.
- 1. Field of the Invention
- The present invention relates to a trivalent chromium plating solution and a plating method using the same, and more particularly, to a hard trivalent chromium plating solution having improved covering power.
- 2. Description of the Related Art
- Chrome plating is the most common process among various plating processes and is a final treatment step. Chrome plating may be classified into decorative plating for obtaining a beautifully glossy metal surface and hard plating for increasing wear resistance.
- In the case of decorative plating, the plating thickness typically ranges from 0.2 to 0.5 μm. Decorative plating is usually used to plate brass surfaces of tableware and other disposable products. In the case of hard plating, the plating thickness may range from approximately 5 to several tens of μm although it varies according to the required wear life. Hard plating is used to prevent a portion of a camera lens to which a screw is tightened, a precision machine, an inner surface of a mold, a surface of a printing plate, etc. from wearing out.
- In hexavalent chromium plating, electroplating is typically performed using a solution of chromic acid (CrO3) mixed with sulfuric acid (H2SO4). For an anode, an element that is not eroded by H2SO4, such as lead, is used instead of chromium metal. Electrodeposition is continuously performed while CrO3 supplement a reduction of chromium in the solution.
- The concentration of CrO3 in a plating solution used for chrome plating may be high or low, and various forms of coatings can be obtained depending on the temperature of the solution and current density, that is, plating conditions. Advantages of hexavalent chromium plating include excellent reflectivity, color and corrosion resistance as well as high current efficiency.
- Despite these advantages, hexavalent chromium plating produces CrO3 gas that is fatal to the human body during the plating process. In particular, hexavalent chromium ions introduced into underground water or rivers may cause deadly environmental contamination. Therefore, hexavalent chromium must be reduced to trivalent chromium.
- That is, hexavalent chromium is classified as a carcinogen by the International Agency of Research on Cancer (IARC). Since the use of hexavalent chromium is expected to be prohibited, alternatives to hexavalent chromium are required. Accordingly, a lot of research is being actively conducted worldwide to develop alternatives to hexavalent chromium.
- Examples of alternatives to hexavalent chromium plating include ion-nitriding, plasma spraying, and ion plating. However, these alternatives require 5 to 10 times the cost of hexavalent chromium plating and cannot be applied to large-sized products.
- For these reasons, chrome plating using trivalent chromium is being recognized as the most efficient alternative.
- However, a conventional trivalent chromium plating solution does not have superior covering power. Thus, it is difficult to apply electroplating on surfaces of machine parts or products having complicated shapes.
- Aspects of the present invention provide a trivalent chromium plating solution having superior covering power.
- However, aspects of the present invention are not restricted to the one set forth herein. The above and other aspects of the present invention will become more apparent to one of ordinary skill in the art to which the present invention pertains by referencing the detailed description of the present invention given below. According to an aspect of the present invention, there is provided a trivalent chromium plating solution comprising a trivalent chromium compound including a compound of formula (1) below;
-
wherein Cr2(SO4)n(OH)6-2n (n<3) (1). - According to another aspect of the present invention, there is provided a plating method comprising preparing a trivalent chromium plating solution in a plating bath, immersing an object to be plated in the trivalent chromium plating solution, and applying a negative potential to the object to be plated and applying a positive potential to an insoluble anode after installing the insoluble anode in the plating bath, wherein the trivalent chromium plating solution comprises a trivalent chromium compound comprising a compound of formula (1) below, a complexing agent suppressing a polymerization reaction of the trivalent chromium compound in the plating solution, a conductivity agent increasing electrical conductivity of trivalent chromium ions, a buffer agent stabilizing a hydrogen ion index of the plating solution, a plating activating additive increasing adhesive power and capability of forming a plated layer, a wetting agent removing a pitting phenomenon which occurs on a plated surface, and a hydrogen ion index adjusting agent adjusting the hydrogen ion index of the plating solution,
-
wherein Cr2(SO4)n(OH)6-2n (n<3) (1). - The above and other aspects and features of the present invention will become more apparent by describing in detail exemplary embodiments thereof with reference to the attached drawings, in which:
-
FIG. 1 is a process flowchart illustrating a method of preparing a trivalent chromium solution according to the present invention; and -
FIG. 2 is a flowchart illustrating a plating process using a trivalent chromium plating solution according to the present invention. - The present invention will now be described more fully hereinafter with reference to the accompanying drawings, in which preferred embodiments of the invention are shown. This invention may, however, be embodied in different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art.
- A trivalent chromium plating solution according to the present invention may include a trivalent chromium compound which provides trivalent chromium ions, a complexing agent which suppresses a polymerization reaction of the trivalent chromium compound in the plating solution, a conductivity agent which increases electrical conductivity of the trivalent chromium ions, a buffer agent which stabilizes a hydrogen ion index of the plating solution, a plating activating agent which increases adhesive power and capability of forming a plated layer, a wetting agent which removes a pitting phenomenon that occurs on a plated surface, and a hydrogen ion index adjusting agent which adjusts the hydrogen ion index of the plating solution.
- The trivalent chromium compound includes a compound of formula (1) below.
-
Cr2(SO4)n(OH)6-2n (n<3) (1). - The trivalent chromium compound may be added to the trivalent chromium plating solution in an amount of 0.4 mol/L to 1.3 mol/L, particularly, 0.8 mol/L to 1 mol/L. Trivalent chromium contained in the trivalent chromium compound forms a chromium film.
- The complexing agent may prevent the trivalent chromium ions contained in the trivalent chromium compound from being polymerized in the plating solution. The complexing agent may be, for example, formic acid, alkali metal formate, or ammonium formate, but is not limited thereto. The complexing agent may be added to the trivalent chromium plating agent in an amount of 0.05 to 2 mol/L, particularly, 0.4 to 0.6 mol/L.
- The conductivity agent may facilitate the formation of a chromium film by increasing electrical conductivity when an object to be plated is immersed in the trivalent chromium plating solution so as to be plated. The conductivity agent may be, for exampe, sodium sulfate, but is not limited thereto. The conductivity agent may be added to the trivalent chromium plating solution in an amount of 0.1 mol/L to 0.8 mol/L, particularly, 0.2 mol/L to 0.4 mol/L.
- The buffer agent enables the hydrogen ion index (pH) of the trivalent chromium plating solution to remain stably within a predetermined range. The buffer agent includes boric acid and aluminium sulfate. As the buffer agent, when both boric acid and aluminium sulfate exist in the trivalent chromium plating solution, high-quality plating can be obtained. Boric acid may be contained in the trivalent chromium plating solution in an amount of 0.08 to 1 mol/L, particularly, 0.4 to 0.6 mol/L. Aluminium sulfate may be contained in the trivalent chromium plating solution in an amount of 0.05 to 0.2 mol/L, particularly, 0.1 to 0.16 mol/L.
- The plating activating agent facilitates plating using low-current, thereby expanding an effective plating current range. The plating activating additive may be, for example, carbamide, but is not limited thereto. The plating activating agent may be contained in the trivalent chromium plating solution in an amount of 0.1 to 1.2 mol/L, particularly, 0.4 to 0.6 mol/L.
- The wetting agent may remove the pitting phenomenon that occurs on a plated surface. The wetting agent may be a surfactant. An example of the surfactant is an organic anion-active surfactant containing a sulfonate group, but is not limited thereto. An example of the organic anion-active surfactant is sodium lauryl sulfate (C12H25SO4Na). The wetting agent may be contained in the trivalent chromium plating solution in an amount of 0.01 to 1 g/L, particularly, 0.05 to 0.1 g/L.
- The hydrogen ion index adjusting agent may adjust the hydrogen ion index of the trivalent chromium plating solution. The hydrogen ion index adjusting agent may be, for example, sulfuric acid (H2SO4), sodium hydroxide (NaOH), or sodium carbonate (Na2CO3), but is not limited thereto. The hydrogen ion index adjusting agent may be added to the trivalent chromium plating solution in an amount that allows the hydrogen ion index of the trivalent chromium plating solution to be in a range of, e.g., 1.1 to 3.5, particularly, 1.4 to 1.8.
- Hereinafter, a method of preparing a trivalent chromium plating solution according to the present invention will be described with reference to
FIG. 1 .FIG. 1 is a process flowchart illustrating a method of preparing a trivalent chromium solution according to the present invention. - Referring to
FIG. 1 , a trivalent chromium compound is added to heated, distilled water and is then stirred (operation S100). Here, the temperature of the distilled water may be approximately 70 to 95° C., and the trivalent chromium compound is stirred until it is completely dissolved in the distilled water. - The solution having the trivalent chromium compound dissolved therein is filtered (operation S110). The solution may be filtered using a paper filter, a fiber filter, or other types of filters.
- A buffer agent and a conductivity agent are added and dissolved in the filtered solution (operation S120). Here, the temperature of the solution may be 70 to 80° C., and the added buffer agent and conductivity agent may be solid. The above solid elements should be completely dissolved in the solution.
- Next, a complexing agent is added to the solution in which the buffer agent and the conductivity agent have been dissolved (operation S130). The solution having the buffer agent and the conductivity agent dissolved therein is maintained at a temperature of 70 to 80° C., and the complexing agent is slowly added to the solution.
- A plating bath is covered with a covering member, and the solution having the complexing agent added thereto is maintained at 70 to 80° C. for a predetermined period of time, for example, for approximately one hour (operation S140).
- Next, the solution maintained at 70 to 80° C. for the predetermined period of time is cooled (operation S150). The solution may be cooled to approximately 40 to 50° C.
- A plating activating agent is added and dissolved in the cooled solution (operation S160). The plating activation agent may be solid and is completely dissolved in the solution at a temperature of 40 to 50° C.
- Then, the plating bath is covered with the covering member, and the solution having the plating activating agent dissolved therein is maintained at a temperature of 40 to 50° C. for a predetermined period of time, for example, for approximately one hour (operation S170).
- The solution maintained at 40 to 50° C. for the predetermined period of time is cooled (operation S180). The solution may be cooled to room temperature.
- The volume of a plating solution is adjusted by adding distilled water to the cooled solution. In addition, a hydrogen ion index of the solution is measured, and, if necessary, the hydrogen ion index of the solution is adjusted by adding a hydrogen ion index adjusting agent to the solution (operation S190).
- Next, a wetting agent is added to the solution having the adjusted hydrogen ion index (operation S200). Specifically, the wetting agent may be added in a predetermined concentration to distilled water, and the distilled water having the wetting agent may be added to the solution having the adjusted hydrogen ion index.
- Distilled water is added to the solution having the wetting agent in order to reach the final volume of the plating solution. Then, the hydrogen ion index of the solution is measured, and, if necessary, the hydrogen ion index of the solution is adjusted again by adding the hydrogen ion index adjusting agent (operation S210).
- Hereinafter, a plating process using a trivalent chromium solution according to the present invention will be described with reference to
FIG. 2 .FIG. 2 is a flowchart illustrating a plating process using a trivalent chromium plating solution according to the present invention. - Referring to
FIG. 2 , a trivalent chromium plating solution according to the present invention is prepared within a plating bath (operation S300). Then, an object to be plated is immersed in the trivalent chromium plating solution (operation S310). - A negative potential is applied to the object to be plated. In addition, an insoluble anode is installed in the plating bath, and a positive potential is applied to the insoluble anode (operation S320). Here, the insoluble anode may be, for example, a titanium-manganese dioxide anode (TMDA), a dimensionally stable anode (DSA) having iridium oxide (IrO2) or ruthenium oxide (RuO2) formed on a porous titanium plate, or a platinized titanium anode, but is not limited thereto. In particular, TMDA does not require spatial separation of a cathode and an anode in a plating process and does not release toxic chlorine gas during the plating process. Furthermore, TMDA noticeably reduces an electrochemical oxidation reaction from trivalent chromium to hexavalent chromium.
- When power is supplied, the current density may be 15 to 30 A/dm2, particularly, 10 to 20 A/dm2.
- During the plating process, a hydrogen ion index of the plating solution may be maintained at 1.1 to 3.5, particularly, 1.4 to 1.8. In addition, the plating bath may be maintained at a temperature of 20 to 60° C., particularly, 30 to 40° C.
- A chromium-plated film may have a thickness of several tens of μm.
- Hereinafter, the present invention will be described in greater detail by way of specific embodiments and a comparative example.
- To prepare 1 L of plating solution, 1 mol of the compound of formula (1) was added to 0.5 to 0.7 L of heated, distilled water and was stirred at 70 to 95° C. until it was completely dissolved.
-
Cr2(SO4)n(OH)6-2n (n<3) (1). - Then, the solution having the compound of formula (1) added thereto was filtered, and 0.15 mol of aluminium sulfate, 0.5 mol of boric acid, and 0.3 mol of sodium sulfate were added to the filtered solution at 70 to 80° C. These added solid elements were completely dissolved. Next, 0.5 mol of formic acid was slowly added to the solution which contained aluminium sulfate, boric acid and sodium sulfate and which was maintained at 70 to 80° C. Then, a plating bath that contained the solution having formic acid added thereto was covered with a covering member and was maintained at 70 to 80° C. for approximately one hour. The solution maintained at 70 to 80° C. for approximately one hour was cooled to 40 to 50° C. After the cooling of the solution, 0.5 mol of solid carbamide was added to the solution being stirred at 40 to 50° C. and was completely dissolved. The plating bath that contained carbamide was covered with the covering member and was maintained at 40 to 50° C. for approximately one hour. Then, the solution maintained at 70 to 80° C. for approximately one hour was cooled to room temperature, and distilled water was added to the cooled solution such that the volume of the plating solution became 0.9 to 0.95 L. Thereafter, a hydrogen ion index of the solution having the distilled water added thereto was measured and, if necessary, was adjusted to 1.5 by adding a H2SO4, NaOH, or Na2CO3 solution to the solution. Using a sodium lauryl sulfate(C12H25SO4Na) solution prepared in a concentration of 10 g/L in advance, 0.1 g of C12H25SO4Na was added to the solution having the adjusted hydrogen ion index. After the addition of C12H25SO4Na, the volume of the plating solution was adjusted to a final volume of 1 L using distilled water. Then, the hydrogen ion index of the solution whose volume had been adjusted to the final volume was measured again and, if necessary, was adjusted to 1.5 by adding the H2SO4, NaOH, or Na2CO3.
- A plating solution was prepared under the same conditions as Embodiment 1, except that the hydrogen ion index was adjusted to 1.7.
- A plating solution was prepared under the same conditions as Embodiment 1, except that the compound of formula (1) was added in an amount of 0.8 mol.
- A plating solution was prepared under the same conditions as Embodiment 1, except that sodium sulfate was added in an amount of 0.2 mol.
- A plating solution was prepared under the same conditions as Embodiment 1, except that the compound of formula (1) was added in an amount of 0.8 mol and that formic acid was added in an amount of 0.4 mol.
- A plating solution was prepared under the same conditions as Embodiment 1, except that carbamide was added in an amount of 0.4 mol and that the hydrogen ion index was adjusted to 1.4.
- A plating solution was prepared by adding 0.5 mol/L of chromium sulfate instead of the compound of formula (1), 0.18 mol/L of aluminium sulfate, 0.63 mol/L of sodium sulfate, 0.45 mol/L of carbamide and 0.66 mol/L of sodium formate. In addition, the hydrogen ion index was adjusted to 1.4.
- The covering power of each of the plating solutions of Embodiments 1 through 6 and Comparative Example 1 was evaluated. Specifically, a disc electrode (S=1.77 cm2) of a copper foil fixed to a plastic holder was used. Electroplating was conducted using TDMA at a constant current density and without the spatial separation of a cathode and an anode. The volume of the plating solution was 0.5 L. The current density was gradually increased by each 1 A/dm2. Electroplating was conducted for 30 seconds for all current density values. A minimum current density when chromium was plated on the whole surface of the cathode was visually determined, and the covering power of the plating solution was measured based on the determination result. The measurement results are shown in Table 1. During the plating process, the temperature of a plating bath was 35° C.
-
TABLE 1 Minimum current density value (A/dm2) that allows a chromium coating to be electro- deposited 100% on a surface of a cathode Comparative Example 1 22 Embodiment 1 15 Embodiment 2 14 Embodiment 3 17 Embodiment 4 19 Embodiment 5 17 Embodiment 6 18 - As apparent from the results shown in Table 1, the minimum current densities of the plating solutions of Embodiments 1 through 6 are far lower than that of the plating solution of Comparative Example 1. Accordingly, the plating solutions of Embodiments 1 through 6 using the trivalent chromium compound of formula (1) have better covering power than the plating solution of Comparative Example 1 using a trivalent chromium compound such as chromium sulfate.
- A trivalent chromium plating solution according to the present invention has superior covering power. In addition, a compound of formula (1), which can also be used as a tanning agent, can be mass-produced and is inexpensive. Therefore, the trivalent chromium plating solution is the first-ever plating solution that provides the compound of formula (1) as a trivalent chromium compound. Using the compound of formula (1) as a source, an economical trivalent chromium plating solution can be produced.
- In concluding the detailed description, those skilled in the art will appreciate that many variations and modifications can be made to the preferred embodiments without substantially departing from the principles of the present invention. Therefore, the disclosed preferred embodiments of the invention are used in a generic and descriptive sense only and not for purposes of limitation.
Claims (14)
1. A trivalent chromium plating solution comprising:
a trivalent chromium compound comprising a compound of formula (1) below;
wherein Cr2(SO4)n(OH)6-2n (n<3) (1).
wherein Cr2(SO4)n(OH)6-2n (n<3) (1).
2. The plating solution of claim 1 , wherein the plating solution further comprising:
a complexing agent suppressing a polymerization reaction of the trivalent chromium compound in the plating solution;
a conductivity agent increasing electrical conductivity of trivalent chromium ions;
a buffer agent stabilizing a hydrogen ion index of the plating solution;
a plating activating agent increasing adhesive power and capability of forming a plated layer;
a wetting agent removing a pitting phenomenon which occurs on a plated surface; and
a hydrogen ion index adjusting agent adjusting the hydrogen ion index of the plating solution,
3. The plating solution of claim 1 , wherein the trivalent chromium compound is added in an amount of 0.4 to 1.3 mol/L.
4. The plating solution of claim 2 , wherein the complexing agent is at least one selected from the group consisted of a formic acid, alkali metal formate and ammonium formate and is added in an amount of 0.05 to 2 mol/L.
5. The plating solution of claim 3 , wherein the conductivity agent is sodium sulfate and is added in an amount of 0.1 to 0.8 mol/L.
6. The plating solution of claim 4 , wherein the buffer agent comprises boric acid and aluminium sulfate, wherein the boric acid is added in an amount of 0.08 to 1 mol/L, and the aluminium sulfate is added in an amount of 0.05 to 0.2 mol/L.
7. The plating solution of claim 5 , wherein the plating activating agent is carbamide and is added in an amount of 0.1 to 1.2 mol/L.
8. The plating solution of claim 6 , wherein the wetting agent is sodium lauryl sulfate and is added in an amount of 0.01 to 1 g/L.
9. The plating solution of claim 7 , wherein the hydrogen ion index adjusting agent may be at least one selected from the group consisted of a sulfuric acid (H2SO4), sodium hydroxide (NaOH), and sodium carbonate (Na2CO3).
10. The plating solution of claim 1 , having a hydrogen ion index of 1.1 to 3.5.
11. A plating method comprising:
preparing a trivalent chromium plating solution in a plating bath;
immersing an object to be plated in the trivalent chromium plating solution; and
applying a negative potential to the object to be plated and applying a positive potential to an insoluble anode after installing the insoluble anode in the plating bath,
wherein the trivalent chromium plating solution comprises:
a trivalent chromium compound comprising a compound of formula (1) below;
a complexing agent suppressing a polymerization reaction of the trivalent chromium compound in the plating solution;
a conductivity agent increasing electrical conductivity of trivalent chromium ions;
a buffer agent stabilizing a hydrogen ion index of the plating solution;
a plating activating additive increasing adhesive power and capability of forming a plated layer;
a wetting agent removing a pitting phenomenon which occurs on a plated surface; and
a hydrogen ion index adjusting agent adjusting the hydrogen ion index of the plating solution,
wherein Cr2(SO4)n(OH)6-2n (n<3) (1).
wherein Cr2(SO4)n(OH)6-2n (n<3) (1).
12. The plating method of claim 11 , wherein the insoluble anode is a titanium-manganese dioxide anode (TMDA), a dimensionally stable anode (DSA) having iridium oxide (IrO2) or ruthenium oxide (RuO2) formed on a porous titanium plate, or a platinized titanium anode.
13. The plating method of claim 11 , wherein in the applying of the negative potential and the applying of the positive potential, a current density is 15 to 30 A/dm2.
14. The plating method of claim 11 , wherein the plating bath is maintained at a temperature of 20 to 60° C.
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| Application Number | Priority Date | Filing Date | Title |
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| KR1020100073495A KR101198353B1 (en) | 2010-07-29 | 2010-07-29 | Trivalent chromium plating solution and plating method using the same |
| KR10-2010-0073495 | 2010-07-29 |
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| US20120024714A1 true US20120024714A1 (en) | 2012-02-02 |
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| US13/188,515 Abandoned US20120024714A1 (en) | 2010-07-29 | 2011-07-22 | Trivalent chromium plating solution and plating method using the same |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US20150252487A1 (en) * | 2014-03-07 | 2015-09-10 | Macdermid Acumen, Inc. | Passivation of Micro-Discontinuous Chromium Deposited From a Trivalent Electrolyte |
| JP2016528378A (en) * | 2013-06-20 | 2016-09-15 | タタ、スティール、アイモイデン、ベスローテン、フェンノートシャップTata Steel Ijmuiden Bv | Method for producing a chromium-chromium oxide coated substrate |
| CN106086949A (en) * | 2016-08-26 | 2016-11-09 | 武汉迪赛环保新材料股份有限公司 | A kind of trivalent chromium plating solution and electro-plating method |
| US20170081773A1 (en) * | 2014-05-21 | 2017-03-23 | Tata Steel Ijmuiden B.V. | Method for plating a moving metal strip and coated metal strip produced thereby |
| US20170314153A1 (en) * | 2016-05-02 | 2017-11-02 | The Boeing Company | Trivalent chromium plating formulations and processes |
| US10000861B2 (en) | 2012-03-30 | 2018-06-19 | Tata Steel Ijmuiden Bv | Coated substrate for packaging applications and a method for producing said coated substrate |
| US10400338B2 (en) | 2017-05-12 | 2019-09-03 | Chemeon Surface Technology, Llc | pH stable trivalent chromium coating solutions |
| CN113774438A (en) * | 2021-08-24 | 2021-12-10 | 上原汽车铭牌(惠州)有限公司 | Trivalent chromium electroplating solution formula for automobile mark production and trivalent chromium electroplating process |
| US20230243057A1 (en) * | 2020-07-15 | 2023-08-03 | Tata Steel Nederland Technology B.V. | Method for electrodepositing a functional or decorative chromium layer from a trivalent chromium electrolyte |
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| KR102280086B1 (en) * | 2018-09-28 | 2021-07-22 | 주식회사 포스코 | Trivalent chromium electroplating solution and electroplating method for using the same |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2999003A (en) * | 1959-02-06 | 1961-09-05 | Du Pont | Leather tanning agent and process |
| US3766028A (en) * | 1971-04-02 | 1973-10-16 | Albright & Wilson | Electrowinning of chromium metal |
| US3954574A (en) * | 1973-12-13 | 1976-05-04 | Albright & Wilson Limited | Trivalent chromium electroplating baths and electroplating therefrom |
| US4157945A (en) * | 1977-03-04 | 1979-06-12 | International Lead Zinc Research Organization, Inc. | Trivalent chromium plating baths |
| US4543167A (en) * | 1982-03-05 | 1985-09-24 | M&T Chemicals Inc. | Control of anode gas evolution in trivalent chromium plating bath |
| US20080169199A1 (en) * | 2007-01-17 | 2008-07-17 | Chang Gung University | Trivalent chromium electroplating solution and an electroplating process with the solution |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102006035871B3 (en) * | 2006-08-01 | 2008-03-27 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Process for the deposition of chromium layers as hard chrome plating, plating bath and hard chrome plated surfaces and their use |
| KR100858711B1 (en) | 2007-03-30 | 2008-09-17 | 한국기계연구원 | Trivalent chromium plating solution |
| KR100970951B1 (en) * | 2008-03-03 | 2010-07-21 | 한국기계연구원 | Decorative Trivalent Chrome Plating Solution |
-
2010
- 2010-07-29 KR KR1020100073495A patent/KR101198353B1/en not_active Expired - Fee Related
-
2011
- 2011-07-22 US US13/188,515 patent/US20120024714A1/en not_active Abandoned
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2999003A (en) * | 1959-02-06 | 1961-09-05 | Du Pont | Leather tanning agent and process |
| US3766028A (en) * | 1971-04-02 | 1973-10-16 | Albright & Wilson | Electrowinning of chromium metal |
| US3954574A (en) * | 1973-12-13 | 1976-05-04 | Albright & Wilson Limited | Trivalent chromium electroplating baths and electroplating therefrom |
| US4157945A (en) * | 1977-03-04 | 1979-06-12 | International Lead Zinc Research Organization, Inc. | Trivalent chromium plating baths |
| US4543167A (en) * | 1982-03-05 | 1985-09-24 | M&T Chemicals Inc. | Control of anode gas evolution in trivalent chromium plating bath |
| US20080169199A1 (en) * | 2007-01-17 | 2008-07-17 | Chang Gung University | Trivalent chromium electroplating solution and an electroplating process with the solution |
Cited By (12)
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|---|---|---|---|---|
| US10000861B2 (en) | 2012-03-30 | 2018-06-19 | Tata Steel Ijmuiden Bv | Coated substrate for packaging applications and a method for producing said coated substrate |
| JP2016528378A (en) * | 2013-06-20 | 2016-09-15 | タタ、スティール、アイモイデン、ベスローテン、フェンノートシャップTata Steel Ijmuiden Bv | Method for producing a chromium-chromium oxide coated substrate |
| US20150252487A1 (en) * | 2014-03-07 | 2015-09-10 | Macdermid Acumen, Inc. | Passivation of Micro-Discontinuous Chromium Deposited From a Trivalent Electrolyte |
| US10415148B2 (en) * | 2014-03-07 | 2019-09-17 | Macdermid Acumen, Inc. | Passivation of micro-discontinuous chromium deposited from a trivalent electrolyte |
| US20170081773A1 (en) * | 2014-05-21 | 2017-03-23 | Tata Steel Ijmuiden B.V. | Method for plating a moving metal strip and coated metal strip produced thereby |
| US10422049B2 (en) * | 2014-05-21 | 2019-09-24 | Tata Steel Ijmuiden B.V. | Method for plating a moving metal strip and coated metal strip produced thereby |
| US20170314153A1 (en) * | 2016-05-02 | 2017-11-02 | The Boeing Company | Trivalent chromium plating formulations and processes |
| CN106086949A (en) * | 2016-08-26 | 2016-11-09 | 武汉迪赛环保新材料股份有限公司 | A kind of trivalent chromium plating solution and electro-plating method |
| US10400338B2 (en) | 2017-05-12 | 2019-09-03 | Chemeon Surface Technology, Llc | pH stable trivalent chromium coating solutions |
| US20230243057A1 (en) * | 2020-07-15 | 2023-08-03 | Tata Steel Nederland Technology B.V. | Method for electrodepositing a functional or decorative chromium layer from a trivalent chromium electrolyte |
| US12359331B2 (en) * | 2020-07-15 | 2025-07-15 | Tata Steel Nederland Technology B.V. | Method for electrodepositing a functional or decorative chromium layer from a trivalent chromium electrolyte |
| CN113774438A (en) * | 2021-08-24 | 2021-12-10 | 上原汽车铭牌(惠州)有限公司 | Trivalent chromium electroplating solution formula for automobile mark production and trivalent chromium electroplating process |
Also Published As
| Publication number | Publication date |
|---|---|
| KR20120011584A (en) | 2012-02-08 |
| KR101198353B1 (en) | 2012-11-09 |
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