US3268307A - Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof - Google Patents
Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof Download PDFInfo
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- US3268307A US3268307A US262191A US26219163A US3268307A US 3268307 A US3268307 A US 3268307A US 262191 A US262191 A US 262191A US 26219163 A US26219163 A US 26219163A US 3268307 A US3268307 A US 3268307A
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- 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
- C25D15/02—Combined electrolytic and electrophoretic processes with charged materials
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Definitions
- This invention is for improvements in or relating to decorative nickel electroplating, and more particularly relates to (1) the electrodeposition of sub-microscopic satin textured to macroscopic stain textured fine-grained nickel plate from semi-bright and bright nickel plating baths containing dispersed therein fine bath-insoluble particles, and (2) to the exceptional corrosion resistance of these deposits when over-laid with a thin chromium plate.
- the decorative fine-grained nickel deposits of this invention have various degrees of brightness, or of uniform smokiness, or of uniform satin-sheen depending mainly on the concentration and particle size of the dispersed fined powders in the semi-bright or bright nickel electroplating baths, the concentration of the nickel brighteners, the degree of agitation of the cathode or the solution, the brightness and smoothness of the metal surfaces plated upon, and the thickness of the plate applied, and these decorative nickel plates of various degrees of submicroscopic, microscopic, and macroscopic satin texture and luster when over-laid with a final thin chromium plate provide exceptionally outstanding corrosion protection to the underlying metal.
- Such improved decorative nickel deposits of this invention may be produced by the addition to semi-bright and bright nickel electroplating baths of water-insoluble fine powders of boron, silicon, and the borides of calcium, magnesium, tantalum, chromium, titanium, zirconium, vanadium, the carbides of chromium, vanadium, tungsten, and zirconium, the nitrides of silicon, titanium, and zirconium, and the silicides of titanium, zirconium, nickel, cobalt, and cerium, the phosphides of chromium, tungsten, molybdenum, manganese, nickel, cobalt, iron, cerium, titanium, zirconium and vanadium, and the oxides of thorium and stannic tin, including hydrated stannic oxide, (meta stannic acid).
- the macroscopic stain textured types of nickel plate which can be obtained by using the higher concentratrons, e.g., about grams/liter or higher of the aforementioned powders in the semi-bright and bright nickel electroplating baths are fine-grained lustrous satin nickel deposits which not only have a very pleasing appearance, but which can also be high-lighted by buffing raised areas to give beautiful two-tone effects, and which when chromium plated with about 0.01 mil chromium plate will also provide exceptionally good corrosion protection to the basis metals such as ferrous, aluminum, magnesium, brass, copper, zinc and other metal articles.
- the average particle diameter (herein sometimes referred to as particle size) of the finely powdered bathinsoluble materials should not be greater than 5 microns. As some roughness, especially on shelf areas where particles can settle, may result from the use of materials of particle size greater than about 5 microns, the use of material of particle sizes less than 5 microns are preferred and are advantageous, with the most preferred particle size averaging about 0.02 to about 3 microns as determined with the electron microscope. Some agglomerated particles may have larger particle size than 5 microns but with agitation in the nickel bath the larger agglomerates may be reduced to 5 microns and under. Agitation is usually necessary to keep the fine powder suspended in the baths during plating. Air agitation or mechanical agitation including ultra-sonic agitation of the baths can be used.
- This textured plate has excellent adhesion, for example, to nickel, ferrous, copper and brass surfaces similar to that obtained when the nickel bath contains none of the powdered material.
- the leveling of the bright nickel plate is not decreased by the presence of the finely powdered additives.
- the throwing and covering power of the agitated bright nickel baths with the suspended powders is about the same as without the fine powders present. It has been found that in plating articles with recessed areas and with shelf areas using particles of the preferred particle size, no objectionable roughness is obtained on the areas on which settling can occur, though in some cases with the larger particle sizes, the shelf areas may be somewhat duller than the rest of the article, though this is usually negligible with short plating times such as 30 seconds to about 5 minutes. With the microscopic satin nickel this dulling is, of course, no problem.
- the fine bath-insoluble powders plate out as uniform dispersions in the semi-bright and bright nickel plate and thereby cause sub-microscopic (with the finest particles of 0.01 to about 0.05 micron size) to micro-inclusions and sub-microscopic to microscopic-pitting in the surface of the nickel plate. That is, at any given instant the surface of the semi-bright or bright nickel plate has distributed over its surface multitudinous fine particles in various stages of being imbedded in the surface and causing sub-microscopic and microscopic pitting, and with the thinnest plates (flashes or strikes) the pitting is mostly sub-microscopic becoming more microscopically visible with thicker plating.
- the penetration of the corrosion pits toward the underlying basis metal is very greatly diminished.
- There is also some evidence of extremely fine stress-cracking of the chromium around the micro-inclusions which is also favorable to forming micro-cathodes and anodes.
- These textured nickel deposits give the best appearance and corrosion protection results when plated on top of semi-bright sulfur-free nickel or bright nickel deposits. It is best and also simpler to use the regular semi-bright or bright nickel plating baths for most of the plate and to use the minimum of the textured nickel plate required to obtain the desired appearance and corrosion resistance because the textured nickel plating bath requires added control due to the presence of the dispersed particles, and also because the best corrosion protection results are obtained in this way.
- the macroscopic satin textured nickel plate obtained from the agitated bright or semi-bright nickel plating baths containing the higher concentrations of these fine powders can, as already mentioned, easily be buffed to a high luster, without losing the exceptional corrosion resistance when chromium plated.
- the beautiful two-tone effects achieved by buffing accessible portions of the macroscopic satin nickel plated object still have the very high corrosion resistance after final chromium plating.
- Another useful decorative effect can be obtained where brush or polishing lines are desired in a satin finish, by using coarse polishing grit, for example, 120 to 150 emery on the basis metal.
- the original coarse polishing lines, although diminished by the high leveling satin nickel plate, are still visible. In this way, a highly corrosion resistant scratch brush finish satin nickel is obtained without having to resort to scratch brushing a final nickel plate and thus greatly decreasing its corrosion protection.
- bright or semi-bright nickel plating baths of the Watts, sulfate, high chloride, sulfamate or fluoborate type, or mixtures can be used. While bori acid is the buffer usually used, other bufi'ers, such as formates, acetates, succinates or citrates may also be employed.
- the pH of the baths may be from about 2 to 6, though the preferred pH values are from about 3.5 to 5.2.
- the temperature of the baths can be from room temperature to at least 80 0, though in general a temperature of about C. to about C. is preferred.
- the best addition agents or brighteners to achieve the semi-bright and bright nickel plating conditions necessary to obtain the lustrous textured nickel after the addition to the bath of the afore-mentioned powders are the following: the sulfur-containing brighteners including aromatic and unsaturated aliphatic sulfonic acids, sulfonamides and sulfonimides, such as the benzeneor naphthalene-sulfonic acids, p-toluene sulfonamide, benzene sulfonamide, o-benzoyl sulfimide, vinyl sulfonic acid, allyl sulfonic acid, 2-butyne-l,4-disulfonic acid, o-sulfobenzaldehylde, etc; the addition agents which produce sernibright sulfur-free nickel plate such as formaldehyde, chloral hydrate, bromal hydrate, coumarin, butyne diol, a
- Cobalt and iron can be present in the nickel bath as cobalt or ferrous sulfates, hlorides, bromides, sulfamates or fluoborates in concentrations as high as at least 40 grams/liter, yielding nickel alloy plates containing concentrations of cobalt and/or iron up to a total of about 50%, and it is to be understood that, except when the context requires otherwise, the expression nickel plate" as used herein covers such nickel alloy plates.
- Surface active agents may be present in the baths, but are not usually necessary in the air agitated baths.
- the maximum increase in lustrous sheen is obtained when the fine powders are used in the agitated full bright nickel plating baths such as the air-agitated bright nickel plating baths possessing good leveling properties. Less luster is obtained when the nickel baths contain only a carrier type brightener such as benzene or naphthaline sulfonic acids, p-toluene sulfonamide, benzene sulfonamide or Tavernzoyl sulfimide. In the latter cases the luster is flatter.
- a carrier type brightener such as benzene or naphthaline sulfonic acids, p-toluene sulfonamide, benzene sulfonamide or Tavernzoyl sulfimide. In the latter cases the luster is flatter.
- the sub-microscopic to macroscopic satin textured nickel accepts chromium plate like regular nickel plate, and in general only the usual thicknesses of final chromium layer need be used, that is 0.25 micron though thicknesses of 2.5 or 5 microns may be used.
- the decorative nickel finish as such, or with the usual final chromium finish the sub-microscopic to macroscopic satin textured nickel plate can be given a rhodium, silver, tin, brass, bronze, copper, gold, or tin-nickel (65-35) alloy or other final thin coating.
- Thin wax, or soluble wax, films or clear lacquers greatly decrease finger marking of the final coatings, such as nickel, bronze, silver, or brass coatings. Chromium, rhodium, and tin-nickel alloy plate do not need these organic coatings, at least not for tarnishing etfects.
- baths of this invention are listed below. It is to be understood that other inorganic bath compositions may be used and other brighteners, though one of the preferred class of brighteners is the organic sulfoncompounds.
- Example I Grams/liter Boron fine powder, 0.02 to 3 microns av. particle size 0.1-250 Ultra-fine silicon dioxide powder (Quso) 1-50 NiSO .6H O 200-300 NiCl .6H O 40-120 H 80 40 o-Benzoy1 sulfimide 1-4 p-Toluene sulfonamide 1-2 Allyl sulfonic acid 1-4 2-butynoxy-1,4-dietl1ane sulfonic acid 0.05-02 pH:3.5-5.2, temp. 50-70 C. Air agitation.
- Example I Silicon fine powder, 0.02 to 5 microns av.
- Example III Thorium oxide fine powder, 0.02 to 3 micron av. particle size 0.2-150 NiSO .6H O 50-200 NiCl bH O 200-100 H BO 40 Benzene sulfonamide 1-3 oBenzoyl sufimide 2-4 Allyl sulfonic acid l-3 N-allyl isoquinoliniurn bromide 0002-001 pH:3.0-5.2, temp. 50-70 C. Air agitation.
- Example V Boron fine powder, 0.02 to 3 micron av. particle size 0.02-5 Silicon dioxide fine powder, 0.02 to 0.5 micron av. ultimate particle size 10-50 NiSO .6H O 200-300 NiCI oI-I O 30-60 H B0 40 Bromal and/or chloral hydrate 005-01 Formaldehyde 0.02-0.08
- the micro-inclusions and micro-pitting can be more easily discerned, and an increasing degree of visible satin texture of the plate occurs.
- the lower concentrations of powder of 0.02 to about 20 grams/liter, and in some cases even to about 50 grams/liter are best for obtaining bright plate from the bright nickel baths, and can thus be used best for very thin plates of about 0.01 to 0.1 mil thickness on top of regular bright nickel or semibright nickel plate to obtain after the final thin chromium plate very high corrosion protecting bright plate.
- the textured plate of this invention is applied on top of regular nickel plate which can be dull, semi-bright or bright nickel plate depending on the decorative effect desired. That is, the degree of brightness, smokiness, or satin quality is dependent on the original brightness and smoothness of the surface plated upon, as Well as the thickness of the plate applied, the concentration and type of brighteners present, the concentration of the powder in the bath, the particle size of the powder and the type of powder, that is, its chemical constitution.
- the nickel brighteners that produce very high leveling and brilliance as, for example, those given in US. 2,647,- 866 (August 4, 1953) and U8. 2,800,440 and 2,800,442 (July 23, 1957) will produce the highest brilliance with the powders dispersed in these bright nickel baths. For less luster, either the higher concentrations of the powders can be used in the very bright plating baths or lower concentrations or with just the organic sulfon-compounds present as brighteners.
- These latter brighteners such as o-benzoyl sulfimide, oor p-toluene sulfonamide naphthalene mono-, dior tri-sulfonic acids, etc., can be used in concentrations ranging from about 0.1 gram/liter to saturation.
- the textured decorative nickel plate of this invention on complex shaped articles such as many zinc die-cast articles, for example, rear view mirror holders, intricate light housings, steel bumpers, hub caps, and grilles, it is best to use duplex or dual nickel underneath the textured nickel deposit.
- the total nickel deposit would consist of semi-bright sulfur-free nickel followed by regular bright nickel followed by a thin textured nickel deposit of this invention.
- the latter being used as thin plate (0.01 to about 0.1 mil) if the highest brilliance is desired, or as a thicker plate with more powder in the bath to obtain a more subdued brightness or satin type of finish if desired.
- the copper plate When ductile copper plate is used under nickel plate that has a final coating of the textured decorative nickel plate of this invention, then the copper plate also helps in the total corrosion resistance unlike the case when copper is used as a substitute for part of the bright nickel thickness in deposits of copper-bright nickel and the usual 0.01 mil thick final chromium. It is believed that this beneficial etfect of copper is also due to the tiny cathode areas developed in the final thin chromium plate, which in turn is due to the fine favorable porosity pattern developed in the thin final chromium plate as a result of its being deposited over a decorative nickel surface containing a rnultitudinous sub-micro to micro-inclusions and submicro to micro-pits of the order of 10 per sq. cm.
- a particularly desirable and extremely corrosion resistant composite plate is formed by electroplating the nickel plate of this invention on the upper layer of the composite nickel coating described and claimed in copending application Ser. No. 103,296, filed Apr. 17, 1961, which is assigned to the assignee of this invention now US. Pat. No. 3,090,733, issued May 21, 1963.
- This composite plate comprises a lower nickel plate plate having an average thickness of about 0.15 mil to about 1.5 mils and an average sulfur content less than about 0.03%, a first overlying electroplate of nickel, or nickel-cobalt alloy containing at least about 50% of nickel and having a thickness of about 0.005 mil to about 0.2 mil and an average sulfur content of about 0.05% to about 0.3%, a second overlying layer of nickel or nickel-cobalt alloy containing at least about 50% nickel having a thickness of about 0.15 mil to about 1.5 mils and an average sulfur content of about 0.02% to about 0.15%, the second overlying layer containing a lower percentage of sulfur than said first overlying nickel electroplate and a higher percentage of sulfur than said lower nickel plate, an overlying layer of the nickel plate of this invention, and a top or upper layer of chromium having a thickness less than about 5 microns.
- the fine grain nickel plate of this invention may vary from a thin flash layer to the thicker plate characterized as the macroscopic satin textured
- a method for electrodepositing a decorative nickel plate which comprises the step of electrolyzing an aqueous acidic solution of at least one nickel salt selected from the group consisting of nickel sulfate, nickel chloride, nickel fluoborate, nickel sulfamate and mixtures of at least one said nickel salt with up to a total of about 40 grams/ liter of at least one salt selected from the group consisting of the sulfates, chlorides, fiuoborates and sulfamates of cobalt and iron, and at least one soluble organic addition agent capable of producing semi-bright to fully bright nickel plate, said solution containing dispersed therein about 0.1 to about 250 grams/liter of at least one material selected from the class consisting of boron and silicon, and the borides of calcium, magnesium, tantalum, chromium, titanium, zirconium and vanadium, the carbides of chromium, vanadium, tungsten and zirconium, the nitrides of silicon, titanium and zirconium,
- a method for electrodepositing a decorative nickel plate which comprises the step of electrolyzing an aqueous acidic solution of at least one nickel salt selected from the group consisting of nickel sulfate, nickel chloride, nickel fiuoborate and nickel sulfamate and at least one soluble organic addition agent capable of producing semibright to fully bright nickel plate, said solution containing dispersed therein about 0.1 to about 250 grams/liter of at least one material selected from the class consisting of boron and silicon, and the borides of calcium, magnesium, tantalum, chromium, titanium, zirconium and vanadium, the carbides of chromium, vanadium, tungsten, Zirconium, the nitrides of silicon, titanium and zirconium, the silicides of.
- at least one nickel salt selected from the group consisting of nickel sulfate, nickel chloride, nickel fiuoborate and nickel sulfamate and at least one soluble organic addition agent capable of producing semibright to fully bright
- titanium, zirconium, nickei, and cobalt the phosphides of chromium, tungsten, molybdenum, manganese, nickel, cobalt, iron, titanium, zirconium and vanadium, and the oxides of stannic tin, said material being in the form of a fine powder having an ultimate particle size of less than about 5 microns average diameter, thereafter plating on said electrodeposited layer an overlayer of a metal selected from the group consisting of chromium, rhodium, silver, tin, brass, bronze, copper, gold, and an alloy consisting of 65 tin and 35 nickel, said overlayer having a thickness in the range of about 0.25 to about 5 microns.
- a composite electroplate on a metal susceptible to atmospheric corrosion which comprises a nickel plate with a chromium overplate, said nickel plate having been electrodeposited from an acidic nickel plating bath containing dissolved therein at least one organic nickel brightencr capable of. producing semi-bright to fully bright nickel plate, and having dispersed in said bath in a concentration of about 0.1 to about 250 grams/liter of at least one type of bath insoluble particles of average ultimate particle size less than about 5 microns, an electrodeposited chromium overlay plate on said nickel plate of less than about 5 microns thickness, said particles in said nickel bath being selected from the group consisting of boron and silicon, and the borides of calcium, magnesium, tantalum, chromium, titanium, zirconium and vanadium, the carbides of chromium, vanadium, tungsten, and zirconium, the nitrides of silicon, titanium and zirconium, the silicides of titanium, zirconium, nickel, and cobalt, the phosphi
- a composite electroplate in accordance with claim 12 wherein said dissolved organic nickel brightener is selected from the group consisting of aromatic and unsaturated sulfonic acids, sulfonamides, and sulfonimides.
- a composite electroplate on a metal surface susceptible to atmospheric corrosion which comprises a lower nickel electroplate having a thickness of about 0.15 mil to about 1.5 mils and an average sulfur content less than about 0.03%, a first overlying layer consisting essentially of an electroplate selected from the group consisting of nickel electroplate and nickel-cobalt alloy clectroplate containing at least about 50% nickel and having a thickness of about 0.005 mil to about 0.2 mil and an average sulfur content of about 0.05% to about 0.3%, a second overlying layer consisting essentially of an electroplate selected from the group consisting of nickel electroplate and nickel-cobalt alloy electroplate containing at least about 50% nickel, and having a thickness of about 0.15 mil to about 1.5 mils and an average sulfur content of about 0.02% to about 0.15%, the said second overlying layer containing a lower percentage of sulfur than the said first overlying nickel electroplate and a higher percentage of sulfur than said nickel plate, an overlying layer of nickel plate electrodepositcd thereon from an acidic nickel plating
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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)
- Other Surface Treatments For Metallic Materials (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Electroplating Methods And Accessories (AREA)
- Paints Or Removers (AREA)
Priority Applications (12)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1051685D GB1051685A (de) | 1963-03-01 | ||
US262200A US3268423A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating |
US262191A US3268307A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof |
US262199A US3268308A (en) | 1963-03-01 | 1963-03-01 | Electrodeposition of a corrosion resistant decorative nickel-chromium coating and products thereof |
US302739A US3268424A (en) | 1963-03-01 | 1963-08-16 | Method of depositing a corrosion resistant composite nickel electroplate |
FR965672A FR92001E (fr) | 1963-03-01 | 1964-02-29 | Procédé de nickelage, bains utilisés et produits obtenus |
DE1521063A DE1521063C3 (de) | 1963-03-01 | 1964-02-29 | Saures galvanisches Nickelbad zum Abscheiden dekorativer feinkörniger, satinbis hochglänzender Überzüge mit verbesserter Korrosionsfestigkeit |
ES297129A ES297129A2 (es) | 1963-03-01 | 1964-03-02 | Metodo de galvanizado de niquel mediante electrodeposito deuna placa de niquel desde un bano. |
NL6402091A NL6402091A (de) | 1963-03-01 | 1964-03-02 | |
NL6409430A NL6409430A (de) | 1963-03-01 | 1964-08-14 | |
FR985299A FR92105E (fr) | 1963-03-01 | 1964-08-14 | Procédé de nickelage, bains utilisés et produits obtenus |
DE1521065A DE1521065C3 (de) | 1963-03-01 | 1964-08-14 | Saures galvanisches Nickelbad zum Abscheiden dekorativer feinkörniger, satin- bis hochglänzender Überzüge mit verbesserter Korrosionsfestigkeit |
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US28219963A | 1963-03-01 | 1963-03-01 | |
US262200A US3268423A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating |
US262191A US3268307A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof |
US262199A US3268308A (en) | 1963-03-01 | 1963-03-01 | Electrodeposition of a corrosion resistant decorative nickel-chromium coating and products thereof |
US302739A US3268424A (en) | 1963-03-01 | 1963-08-16 | Method of depositing a corrosion resistant composite nickel electroplate |
Publications (1)
Publication Number | Publication Date |
---|---|
US3268307A true US3268307A (en) | 1966-08-23 |
Family
ID=27540443
Family Applications (4)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US262191A Expired - Lifetime US3268307A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating and products thereof |
US262199A Expired - Lifetime US3268308A (en) | 1963-03-01 | 1963-03-01 | Electrodeposition of a corrosion resistant decorative nickel-chromium coating and products thereof |
US262200A Expired - Lifetime US3268423A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating |
US302739A Expired - Lifetime US3268424A (en) | 1963-03-01 | 1963-08-16 | Method of depositing a corrosion resistant composite nickel electroplate |
Family Applications After (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US262199A Expired - Lifetime US3268308A (en) | 1963-03-01 | 1963-03-01 | Electrodeposition of a corrosion resistant decorative nickel-chromium coating and products thereof |
US262200A Expired - Lifetime US3268423A (en) | 1963-03-01 | 1963-03-01 | Process of electrodepositing a corrosion resistant nickel-chromium coating |
US302739A Expired - Lifetime US3268424A (en) | 1963-03-01 | 1963-08-16 | Method of depositing a corrosion resistant composite nickel electroplate |
Country Status (4)
Country | Link |
---|---|
US (4) | US3268307A (de) |
DE (2) | DE1521063C3 (de) |
GB (1) | GB1051685A (de) |
NL (2) | NL6402091A (de) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3428441A (en) * | 1965-07-28 | 1969-02-18 | Kewanee Oil Co | Article coated with a composite particulate,microporous chromium coating and method of producing said article |
US3471271A (en) * | 1965-08-16 | 1969-10-07 | Udylite Corp | Electrodeposition of a micro-cracked corrosion resistant nickel-chromium plate |
US3625821A (en) * | 1968-06-26 | 1971-12-07 | Westinghouse Electric Corp | Fuel-element coating containing burnable poison |
US3657080A (en) * | 1968-09-25 | 1972-04-18 | M & T Chemicals Inc | Mist suppression in electroplating solutions |
US3866289A (en) * | 1969-10-06 | 1975-02-18 | Oxy Metal Finishing Corp | Micro-porous chromium on nickel-cobalt duplex composite plates |
US6045682A (en) * | 1998-03-24 | 2000-04-04 | Enthone-Omi, Inc. | Ductility agents for nickel-tungsten alloys |
WO2006082218A1 (de) * | 2005-02-04 | 2006-08-10 | Siemens Aktiengesellschaft | Oberfläche mit einer die benetzbarkeit vermindernden mikrostruktur und verfahren zu deren herstellung |
CN111926354A (zh) * | 2020-10-12 | 2020-11-13 | 江西科技学院 | 一种计算机数据处理装置用电气元件及其制造方法 |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3356467A (en) * | 1964-12-28 | 1967-12-05 | Udylite Corp | Article coated with a coelectrodeposit of nickel and plastic particles, an overlayerthereon, and method of making said article |
GB1118167A (en) * | 1965-10-23 | 1968-06-26 | Res Holland Nv | Improvements in or relating to the production of microporous chromium deposits |
US3488263A (en) * | 1968-04-22 | 1970-01-06 | Gen Electric | Codeposition of metallics and non-metallics |
GB1282373A (en) * | 1969-10-15 | 1972-07-19 | A I C Approvvigionamenti Ind C | Nickel-chromium electroplating |
GB1404855A (en) * | 1971-07-28 | 1975-09-03 | Mitsui Mining & Smelting Co | Catalytic purification of exhaust gases |
US3812566A (en) * | 1972-07-03 | 1974-05-28 | Oxy Metal Finishing Corp | Composite nickel iron electroplate and method of making said electroplate |
DE2236443C3 (de) * | 1972-07-25 | 1978-05-24 | Elektroschmelzwerk Kempten Gmbh, 8000 Muenchen | Wäßriges Bad zur Herstellung von metallischen Überzügen, die nichtmetallische, feinverteilte Feststoffe eingelagert enthalten |
US3825478A (en) * | 1972-10-30 | 1974-07-23 | Oxy Metal Finishing Corp | Electrolyte and method for electrodepositing microporous chromium-nickel composite coatings |
JPS5618080B2 (de) * | 1973-08-14 | 1981-04-25 | ||
US4182412A (en) * | 1978-01-09 | 1980-01-08 | Uop Inc. | Finned heat transfer tube with porous boiling surface and method for producing same |
US4470897A (en) * | 1983-09-20 | 1984-09-11 | Bethlehem Steel Corp. | Method of electroplating a corrosion-resistant zinc-containing deposit |
CA1268139A (en) * | 1984-10-05 | 1990-04-24 | John Foster | Composite electrodeposition including particles of craim.sub.2 where m.sub.2is y, si, ti or rare earth |
JPH0772360B2 (ja) * | 1987-07-10 | 1995-08-02 | 日本鋼管株式会社 | Zn系複合電気めつき鋼板 |
DE102007060906B3 (de) * | 2007-12-14 | 2009-10-15 | Ab Skf | Lageranordnung für eine Tragrolle |
ATE462025T1 (de) * | 2008-07-15 | 2010-04-15 | Atotech Deutschland Gmbh | Lösung und verfahren zur elektrochemischen abscheidung eines metalls auf ein substrat |
DE102010055968A1 (de) | 2010-12-23 | 2012-06-28 | Coventya Spa | Substrat mit korrosionsbeständigem Überzug und Verfahren zu dessen Herstellung |
WO2013025352A1 (en) | 2011-08-18 | 2013-02-21 | Apple Inc. | Anodization and plating surface treatments |
KR20130126233A (ko) * | 2012-05-11 | 2013-11-20 | 현대자동차주식회사 | 음각처리를 이용한 도금방법 |
GB201308473D0 (en) * | 2013-05-10 | 2013-06-19 | Authentix Inc | Plating of articles |
CN109107559B (zh) * | 2018-08-31 | 2021-08-03 | 四川文理学院 | 一种电沉积制备钛酸钙的方法及其应用 |
CN116005157B (zh) * | 2022-12-13 | 2023-12-19 | 苏州圆格电子有限公司 | 一种钕铁硼表面预处理方法和系统 |
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US2739085A (en) * | 1953-03-13 | 1956-03-20 | Westinghouse Electric Corp | Insulating coatings for magnetic sheets |
US2771409A (en) * | 1953-02-19 | 1956-11-20 | Gen Motors Corp | Method of making grid bearings |
US3057048A (en) * | 1958-11-06 | 1962-10-09 | Horizons Inc | Protection of niobium |
US3061525A (en) * | 1959-06-22 | 1962-10-30 | Platecraft Of America Inc | Method for electroforming and coating |
US3090733A (en) * | 1961-04-17 | 1963-05-21 | Udylite Res Corp | Composite nickel electroplate |
US3132928A (en) * | 1962-02-26 | 1964-05-12 | Donald D Crooks | Simultaneous brazing and corrosion protecting refractory metals |
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US2849353A (en) * | 1955-02-08 | 1958-08-26 | Hanson Van Winkle Munning Co | Bright nickel plating |
-
0
- GB GB1051685D patent/GB1051685A/en active Active
-
1963
- 1963-03-01 US US262191A patent/US3268307A/en not_active Expired - Lifetime
- 1963-03-01 US US262199A patent/US3268308A/en not_active Expired - Lifetime
- 1963-03-01 US US262200A patent/US3268423A/en not_active Expired - Lifetime
- 1963-08-16 US US302739A patent/US3268424A/en not_active Expired - Lifetime
-
1964
- 1964-02-29 DE DE1521063A patent/DE1521063C3/de not_active Expired
- 1964-03-02 NL NL6402091A patent/NL6402091A/xx unknown
- 1964-08-14 NL NL6409430A patent/NL6409430A/xx unknown
- 1964-08-14 DE DE1521065A patent/DE1521065C3/de not_active Expired
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US2771409A (en) * | 1953-02-19 | 1956-11-20 | Gen Motors Corp | Method of making grid bearings |
US2739085A (en) * | 1953-03-13 | 1956-03-20 | Westinghouse Electric Corp | Insulating coatings for magnetic sheets |
US3057048A (en) * | 1958-11-06 | 1962-10-09 | Horizons Inc | Protection of niobium |
US3061525A (en) * | 1959-06-22 | 1962-10-30 | Platecraft Of America Inc | Method for electroforming and coating |
US3090733A (en) * | 1961-04-17 | 1963-05-21 | Udylite Res Corp | Composite nickel electroplate |
US3132928A (en) * | 1962-02-26 | 1964-05-12 | Donald D Crooks | Simultaneous brazing and corrosion protecting refractory metals |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3428441A (en) * | 1965-07-28 | 1969-02-18 | Kewanee Oil Co | Article coated with a composite particulate,microporous chromium coating and method of producing said article |
US3471271A (en) * | 1965-08-16 | 1969-10-07 | Udylite Corp | Electrodeposition of a micro-cracked corrosion resistant nickel-chromium plate |
US3625821A (en) * | 1968-06-26 | 1971-12-07 | Westinghouse Electric Corp | Fuel-element coating containing burnable poison |
US3657080A (en) * | 1968-09-25 | 1972-04-18 | M & T Chemicals Inc | Mist suppression in electroplating solutions |
US3866289A (en) * | 1969-10-06 | 1975-02-18 | Oxy Metal Finishing Corp | Micro-porous chromium on nickel-cobalt duplex composite plates |
US6045682A (en) * | 1998-03-24 | 2000-04-04 | Enthone-Omi, Inc. | Ductility agents for nickel-tungsten alloys |
WO2006082218A1 (de) * | 2005-02-04 | 2006-08-10 | Siemens Aktiengesellschaft | Oberfläche mit einer die benetzbarkeit vermindernden mikrostruktur und verfahren zu deren herstellung |
CN111926354A (zh) * | 2020-10-12 | 2020-11-13 | 江西科技学院 | 一种计算机数据处理装置用电气元件及其制造方法 |
Also Published As
Publication number | Publication date |
---|---|
DE1521065A1 (de) | 1969-08-07 |
US3268308A (en) | 1966-08-23 |
DE1521065B2 (de) | 1973-04-12 |
NL6409430A (de) | 1965-02-17 |
US3268423A (en) | 1966-08-23 |
DE1521063A1 (de) | 1969-08-14 |
NL6402091A (de) | 1964-09-02 |
DE1521065C3 (de) | 1974-11-07 |
DE1521063B2 (de) | 1974-01-10 |
GB1051685A (de) | |
DE1521063C3 (de) | 1974-08-29 |
US3268424A (en) | 1966-08-23 |
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Legal Events
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Owner name: HOOKER CHEMICALS & PLASTICS CORP. Free format text: MERGER;ASSIGNOR:OXY METAL INDUSTRIES CORPORATION;REEL/FRAME:004075/0885 Effective date: 19801222 |
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Owner name: OCCIDENTAL CHEMICAL CORPORATION Free format text: CHANGE OF NAME;ASSIGNOR:HOOKER CHEMICAS & PLASTICS CORP.;REEL/FRAME:004126/0054 Effective date: 19820330 |
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Owner name: OMI INTERNATIONAL CORPORATION, 21441 HOOVER ROAD, Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:OCCIDENTAL CHEMICAL CORPORATION;REEL/FRAME:004190/0827 Effective date: 19830915 |
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Owner name: MANUFACTURERS HANOVER TRUST COMPANY, A CORP OF NY Free format text: SECURITY INTEREST;ASSIGNOR:INTERNATIONAL CORPORATION, A CORP OF DE;REEL/FRAME:004201/0733 Effective date: 19830930 |