EP2451997A1 - Nickel system - Google Patents
Nickel systemInfo
- Publication number
- EP2451997A1 EP2451997A1 EP10742444A EP10742444A EP2451997A1 EP 2451997 A1 EP2451997 A1 EP 2451997A1 EP 10742444 A EP10742444 A EP 10742444A EP 10742444 A EP10742444 A EP 10742444A EP 2451997 A1 EP2451997 A1 EP 2451997A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- nickel
- electrolyte according
- nickel electrolyte
- layers
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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
- C25D3/12—Electroplating: Baths therefor from solutions of nickel or cobalt
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D15/00—Electrolytic or electrophoretic production of coatings containing embedded materials, e.g. particles, whiskers, wires
-
- 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
- C25D21/10—Agitating of electrolytes; Moving of racks
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/1266—O, S, or organic compound in metal component
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/12—All metal or with adjacent metals
- Y10T428/12493—Composite; i.e., plural, adjacent, spatially distinct metal components [e.g., layers, joint, etc.]
- Y10T428/1266—O, S, or organic compound in metal component
- Y10T428/12667—Oxide of transition metal or Al
Definitions
- the present invention relates to a nickel electrolyte and its use.
- Galvanic nickel electrolytes are known to the person skilled in the art in various designs.
- components are provided with copper layers for the surface finishing, the layers with typically two or three nickel ⁇ and a layer of chromium or other alloys are provided. While the outer layers serve the visual appearance of the component, the lower layers essentially serve as corrosion protection.
- Typical applications are, for example, panels, strips, condenser ⁇ protective grids on automobiles.
- nickel electrolytes are based on what is known as Watts 's electrolyte, which typically has the following composition:
- nickel layers are essentially made up of microcracked and microporous layers.
- microcracked layers the deposition of nickel by the use of organic acids creates stresses. A micrograph of such a layer is shown in FIG. The cracks in the nickel layer continue in the chromium deposited thereon. Corrosive attacks are thereby transmitted from the outer chromium layer to the inner nickel layer and do not affect the surface.
- Microporous layers have displaced the microcracked layers in many areas. In microporous layers in addition to sulfur compounds and solids are used, but no organic acids.
- FIG. 4 shows a photograph of a microporous layer.
- No. 3,471,271 describes a process in which cracks are produced in the nickel layer by adding large amounts of solids.
- the object of the present invention was to provide nickel electrolytes with which coatings with other, preferably improved, corrosion properties can be obtained.
- Suitable nickel compounds are various nickel salts, in particular nickel chloride, nickel acetate, nickel sulfate and mixtures thereof.
- the amount of nickel in the nickel electrolyte is preferably 5 to 300 g / L, with an amount of 200 to 280 g / L, each calculated to NiCl, being preferred.
- Particularly suitable organic acids are low molecular weight organic acids such as formic acid, acetic acid, propionic acid, butyric acid and about this. Suitable amounts of the acid are about 5 to 150 g / l, preferably 10 to 30 g / l or 40 to 70 g / l.
- the nickel electrolyte according to the invention contains an inorganic solid, for example aluminum oxide, silicon dioxide, silicates such as, for example, talc, silicon carbide or mixtures thereof.
- Preferred contents of the inorganic solid are in the range of 0.1 to 0.8 g / l, with an amount of 0.1 to 0.3 g / l being preferred.
- the nickel electrolyte preferably contains more than 0.1 g / l of solids, for example 0.15 g / l or 0.2 g / l.
- the nickel electrolyte contains less than 0.8 g / L or less than 0.7 g / L, more preferably less than 0.5 g / L, and more preferably less than 0.4 g / L or less than 0.3 g / l.
- the amount of inorganic solids may also be 0.05 g / L to 100 g / L or 0.1 to 60 g / L.
- average particle size of the inorganic solid (d50) preference is given to using particle sizes of from 0.1 to 3 ⁇ m, more preferably from 0.8 to 3 ⁇ m, even more preferably from 1 to 2.2 ⁇ m.
- the mean grain size may be in the range of 200 nm to 5 ⁇ m or 0.8 to 3 ⁇ m.
- inorganic particles are incorporated in the layer.
- the result is a microcracked layer containing embedded inorganic particles.
- the corresponding layers obtained have hitherto not been known to the person skilled in the art.
- the nickel electrolyte may contain conventional further ingredients of electrolytes, in particular wetting agents, buffer substances and / or brighteners. In one embodiment, the nickel electrolyte additionally contains ammonia. In one embodiment of the invention, the nickel electrolyte according to the invention contains no boric acid. It is preferred that the content of boric acid is ⁇ 10 g / L, more preferably ⁇ 5 g / L, even more preferably ⁇ 1 g / L.
- the nickel electrolyte according to the invention contains no reducing agent such as hypophosphite, as it is used for electroless deposition.
- the content of reducing agent is preferably ⁇ 10 g / l, more preferably ⁇ 5 g / l, even more preferably ⁇ 1 g / l.
- Reducing agent is a means that can reduce Ni 2+ from Ni to Ni.
- the nickel electrolyte according to the invention is preferably adjusted to an acidic pH between pH 1.5 and 6.5, more preferably 2 to 5, and even more preferably 3 to 4.5. This can be done in the usual way by adding acids or alkalis.
- the invention also provides a process for electroplating a component comprising the step of contacting the component with the nickel electrolyte according to the invention and applying a current density of 2 to 15, preferably 5 to 10 A / dm 2 at a temperature of 20 to 55, preferably 25 to 35 ° C.
- a nickel electrolyte is used which already leads to a microcracked structure without the addition of solid, regardless of how the further treatment of the electrolyte is carried out, for example whether the further treatment of the layer involves hot or cold rinsing.
- Layer thicknesses of more than 2 ⁇ m up to 5 ⁇ m are particularly preferred.
- the chrome layer thickness shows less influence.
- Chromium layer thicknesses in the range of about 0.375 to 2 microns are suitable.
- Electroplating with nickel electrolytes is known in principle to a person skilled in the art and customary process measures for plating with nickel electrolytes are also applicable to the novel electrolyte according to the invention.
- the new electrolyte By using the new electrolyte, a special structure is obtained which has defined pores and cracks. Surprisingly, this leads to a significant change in the corrosion properties.
- the component being electroplated is plastic or metal.
- one or more copper layers are applied, which are then coated by one or more nickel layers and finally by decorative layers, for example chrome layers.
- At least one of the nickel layers is a nickel layer according to the invention.
- the nickel electrolyte according to the invention can advantageously be applied with conventional galvanic equipment, so that no structural measures are required.
- the invention furthermore relates to a component which has one or more layers obtainable by the process according to the invention.
- FIG. 1 shows the results of a CASS test with components coated according to Comparative Example 1 (back) and Comparative Example 2 (front).
- Figure 2 shows results of a test against calcium chloride salts based on kaolin pastes. A component with a coating according to Example 2 (top) with a coating according to Comparative Example 1 (bottom) was compared.
- FIG. 3 shows a photograph of a microcracked layer of the prior art.
- Figure 4 shows a microporous layer according to the prior art.
- Figure 5 shows a structure obtained with the nickel electrolyte of the present invention.
- FIG. 6 shows a surface image obtained with that of the electrolyte according to the invention, but without the addition of an inorganic solid.
- FIG. 7 shows a scanning electron micrograph without solids of the surface according to FIG. 6.
- FIG. 8 shows a scanning electron micrograph of the layers according to the invention with a built-in solid.
- FIG. 9 shows a coating as obtained with an electrolyte of US Pat. No. 3,471,271 Example 1 (without addition of solid).
- FIG. 10 shows, under identical conditions, the deposition of an electrolyte according to the invention according to Example 2 (without addition of solid).
- the layers according to the invention show improved corrosion resistance, in particular in the corrosion of calcium chloride as road salt.
- Calcium chloride has a lower dew point than other salts and is extremely active due to its strong hyposcopic behavior.
- the widespread microporous chromium coatings are often attacked clearly visible already after a winter.
- Nickel chloride 45 g / l
- Brightening additive 0.5 ml / l
- the coating produced shows a solids-dependent microporous surface with at least 8,000 pores / cm 2 .
- Nickel chloride 250 g / l
- Brightening additive 1 ml / l
- the coating shows a defined, coherent structure combination with increased surface area and micropores.
- Nickel chloride 180 g / l
- Brightening additive 0.5 ml / l
- Nickel chloride 210 g / l
- Nickel sulfate 44 g / l
- Brightening additive 1.0 ml / l
- the coating shows a defined, coherent structure combination with an enlarged surface area and micropores.
- CASS test copper accelerated acidic salt spray test
- DIN 50021 The CASS test (copper accelerated acidic salt spray test) is described in DIN 50021.
- test pieces are sprayed with a saline solution of the following composition: - 50 g / l sodium chloride
- the part is removed from the mist, rinsed thoroughly and dried.
- the dissolved copper salt causes a dissolution of the least noble metal in the layer system.
- the CASS test shows the corrosion path in the layer system.
- Figure 1 shows the results of the CASS test after 96 h.
- the rear component, coated according to Comparative Example 1 shows corrosion phenomena can be seen, while the component with a coating according to Example 2 (front) shows no signs of corrosion.
- a paste is prepared from 5 ml of saturated calcium chloride solution and 3 g of kaolin and a pH of 6.5 to 7.5. It is a mushy substance. A defined amount is applied to a sample body in a suitable diameter and stored at 60 0 C for 48 h. This is an accelerated test for assessing resistance to calcium chloride-containing road salt.
- FIG. 2 shows that the component coated in accordance with Comparative Example 1 (front) shows marked traces of corrosion, while the part coated according to the invention (rear) shows no signs of corrosion.
- FIG. 9 shows that the structure has no cracks without addition of solid.
Landscapes
- 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
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP10742444.2A EP2451997B1 (en) | 2009-07-07 | 2010-07-07 | Nickel electrolyte |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09164714 | 2009-07-07 | ||
EP10742444.2A EP2451997B1 (en) | 2009-07-07 | 2010-07-07 | Nickel electrolyte |
PCT/EP2010/059761 WO2011003957A1 (en) | 2009-07-07 | 2010-07-07 | Nickel system |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2451997A1 true EP2451997A1 (en) | 2012-05-16 |
EP2451997B1 EP2451997B1 (en) | 2013-12-25 |
Family
ID=41334602
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10742444.2A Not-in-force EP2451997B1 (en) | 2009-07-07 | 2010-07-07 | Nickel electrolyte |
Country Status (6)
Country | Link |
---|---|
US (1) | US20120164479A1 (en) |
EP (1) | EP2451997B1 (en) |
CN (1) | CN102482792A (en) |
ES (1) | ES2452867T3 (en) |
MX (1) | MX2012000241A (en) |
WO (1) | WO2011003957A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105002525A (en) * | 2015-08-21 | 2015-10-28 | 无锡桥阳机械制造有限公司 | Semi-bright nickel plating solution |
EP3147389B1 (en) | 2015-09-25 | 2019-04-17 | MacDermid Enthone GmbH | Multicorrosion protection system for decorative parts with chrome finish |
JP6760166B2 (en) * | 2017-03-23 | 2020-09-23 | トヨタ自動車株式会社 | A method for forming a nickel film and a nickel solution for use in the method. |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3471271A (en) * | 1965-08-16 | 1969-10-07 | Udylite Corp | Electrodeposition of a micro-cracked corrosion resistant nickel-chromium plate |
US3825478A (en) * | 1972-10-30 | 1974-07-23 | Oxy Metal Finishing Corp | Electrolyte and method for electrodepositing microporous chromium-nickel composite coatings |
US5217536A (en) * | 1990-06-06 | 1993-06-08 | C. Uyemura & Co., Ltd. | Composite plating apparatus |
US5342502A (en) * | 1992-08-31 | 1994-08-30 | Industrial Technology Research Institute | Method of preparing silicon carbide particles dispersed in an electrolytic bath for composite electroplating of metals |
-
2010
- 2010-07-07 ES ES10742444.2T patent/ES2452867T3/en active Active
- 2010-07-07 US US13/382,644 patent/US20120164479A1/en not_active Abandoned
- 2010-07-07 CN CN201080032258XA patent/CN102482792A/en active Pending
- 2010-07-07 WO PCT/EP2010/059761 patent/WO2011003957A1/en active Application Filing
- 2010-07-07 EP EP10742444.2A patent/EP2451997B1/en not_active Not-in-force
- 2010-07-07 MX MX2012000241A patent/MX2012000241A/en unknown
Non-Patent Citations (1)
Title |
---|
See references of WO2011003957A1 * |
Also Published As
Publication number | Publication date |
---|---|
CN102482792A (en) | 2012-05-30 |
ES2452867T3 (en) | 2014-04-03 |
EP2451997B1 (en) | 2013-12-25 |
MX2012000241A (en) | 2012-06-01 |
WO2011003957A1 (en) | 2011-01-13 |
US20120164479A1 (en) | 2012-06-28 |
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