US3445355A - Method and composition for the electrolytic etching of beryllium-copper alloys - Google Patents
Method and composition for the electrolytic etching of beryllium-copper alloys Download PDFInfo
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- US3445355A US3445355A US565386A US3445355DA US3445355A US 3445355 A US3445355 A US 3445355A US 565386 A US565386 A US 565386A US 3445355D A US3445355D A US 3445355DA US 3445355 A US3445355 A US 3445355A
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- etching
- beryllium
- small amount
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Links
- 239000000203 mixture Substances 0.000 title claims description 20
- 238000000034 method Methods 0.000 title claims description 11
- 229910000881 Cu alloy Inorganic materials 0.000 title description 17
- DMFGNRRURHSENX-UHFFFAOYSA-N beryllium copper Chemical compound [Be].[Cu] DMFGNRRURHSENX-UHFFFAOYSA-N 0.000 title description 15
- 238000000866 electrolytic etching Methods 0.000 title description 5
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 39
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 30
- 239000003792 electrolyte Substances 0.000 claims description 19
- WTDHULULXKLSOZ-UHFFFAOYSA-N Hydroxylamine hydrochloride Chemical compound Cl.ON WTDHULULXKLSOZ-UHFFFAOYSA-N 0.000 claims description 16
- 238000005530 etching Methods 0.000 claims description 14
- 239000002253 acid Substances 0.000 claims description 13
- 229910000892 beryllide Inorganic materials 0.000 claims description 9
- 229910017052 cobalt Inorganic materials 0.000 claims description 8
- 239000010941 cobalt Substances 0.000 claims description 8
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 8
- 239000000243 solution Substances 0.000 description 6
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 239000010935 stainless steel Substances 0.000 description 5
- 229910001220 stainless steel Inorganic materials 0.000 description 5
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- 229910001004 magnetic alloy Inorganic materials 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910001096 P alloy Inorganic materials 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 2
- 239000010953 base metal Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- LHLROOPJPUYVKD-UHFFFAOYSA-N iron phosphanylidynenickel Chemical compound [Fe].[Ni]#P LHLROOPJPUYVKD-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 210000003739 neck Anatomy 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 229910000765 intermetallic Inorganic materials 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25F—PROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
- C25F3/00—Electrolytic etching or polishing
- C25F3/02—Etching
Definitions
- the present invention relates to a method and electrolyte composition for electrolytically etching metal alloys.
- the invention is concerned with the electrolytic etching of beryllium-copper alloys, especially beryllium-copper alloys containing cobalt in the form of cobalt-beryllide.
- beryllium-copper alloys contain cobalt.
- grains of the intermetallic compound cobalt beryllide are formed in a matrix of copper.
- the resulting two-phased system is difiicult to smooth or polish by conventional electrolytic etching techniques.
- the major diificulty is that the anodic potentials established at the surfaces of the two phases result in a preferential dissolution of one of the phases.
- the other phase protrudes at surfaces and edges and this results in a rough surface, rather than the desired smooth surface.
- the objective of the present invention is to provide an electrolyte composition and method for smoothly etching beryllium-copper alloys, especially beryllium-copper alloys containing cobalt beryllide.
- a further specific objective of the invention is to provide a composition and method for electrolytically smoothing beryllium-copper alloys containing grains of copper beryllide.
- the present invention comprises anodically etching an article of a beryllium-copper alloy containing cobalt-beryllide grains to provide a smooth surface on the article by connecting the article as anode in an electrolytic system including an electrolyte containing the following constituents:
- hydrofiuosilicic acid H SiF ethylene glycol, hydroxylamine hydrochloride, isopropyl alcohol, and
- Hydrofluosilicic acid considering, for example, a bath of about 105 ml. volume, comprises the major portion by volume of the composition, generally over 50% and usually on the order of about 60% by volume.
- the hydrofiuosilicic acid is used as 30% by weight aqueous H SiF Ethylene glycol is present in a substantial but minor proportion, generally on the order of about 20% by volume of the composition.
- the hydroxylamine hydrochloride is present in a small amount, generally on the order of 1 gm. and preferably about 0.5 gm.
- the 2,2 diquinoline also is present in a small amount, usually less than 1 gm. and preferably about 0.2 gm. and is dissolved in the isopropyl alcohol.
- the isopropyl alcohol is present in minor proportions which may comprise about 20% by volume of the composition.
- the anodic current density on the surface of the part etched with this composition is preferably in the range "ice of from about 500 to 1000 amperes per square foot (a.s.f.).
- EXAMPLE 1 A part of beryllium-copper alloy which has been precipitation-hardened to form grains of cobalt-beryllide in a matrix of copper was anodically connected in an electrolytic cell which also included a stainless steel cathode plate opposite the part. An electrolyte of the following formulation was introduced into the cell:
- the distribution of current over the surface of the part electrolytically etched can be adjusted to effect overall uniform attack. This is accomplished by the use of shaped cathodes, current shields and current thieves.
- Addition agents can be included in the bath formulation to alter electrical conductivity and solution viscosity as well as the composition of the film at the anode surfaces. The above factors are determined experimentally for each system and part configuration.
- An electrolyte comprising a major portion of hydrofluosilicic acid and a minor portion of ethylene glycol, not including the other above-described additives, has also been found to be useful for through-etching of Be-Cu alloys and for etching Ni-Fe-P magnetic alloy films.
- Beryllium-copper alloys have been found to be useful in the production of substrates for electrical components.
- the metal sheets are suitably masked and etched through their entire thicknesses to form chainlike structures.
- the conventional process for accomplishing the etching has involved exposure to aqueous chemical solutions, such as acidified ferric chloride or ammonium persulfate.
- the rate of dissolution, however, in such chemical etchants is influenced by the concentration of the solution, the presence of dissolved copper salts, and the temperature of the solution, as well as the degree of agitation of the solution.
- one part may be etched properly and another part over-etched or under-etched due to slight variation in conditions.
- the part to be etched is a piece of berylliumcopper alloy which is to be etched completely through at one or more points
- the part is first provided with a coating of a suitable masking or resist material to confine the etching to the desired portions of the base metal.
- the part is then positioned between two cathodes which may be copper or stainless steel sheets and is connected as the anode in the system.
- the electrolyte is then introduced into the cell and an anodic current density of at least 50 a.s.f. is applied.
- the preferred electrolyte is an aqueous solution of hydrofiuosilicic acid and ethylene glycol.
- the preferred cathode material is stainless steel sheet or foil and the anodic current density on the part is preferably in the range of from 500 to 2000 a.s.f.
- Examples 2 and 3 illustrate the above-described electrolytic etching of Be-Cu and Ni-Fe-P alloys.
- EXAMPLE 2 A piece of beryllium-copper alloy 0.003 inch thick is anodically connected between two stainless steel cathodes. The sheet is provided with resist coated areas on those portions of the surface which are not be to etched. An anodic current density of 500 a.s.f. is applied to the part for two minutes in an electrolyte comprising 125 ml. (30% by weight of H SiF and 25 ml. of reagent grade ethylene glycol.
- the extent and rate of removal of the base metal is not influenced by small changes in solution temperature.
- the amount of metal removal can be ascertained and controlled through the use of Ampere-hour meters.
- the rate of penetration is directly related to the current density selected.
- EXAMPLE 3 A thin film of nickel-iron-phosphorus magnetic alloy was deposited on a palladium coated beryllium-copper alloy. Magnetic alloy bits, in a density of 36 bits to a word line, were protected with a resist material. The necks between the covered or protected bits were then etched by immersing the part as an anode in an electrolytic cell containing a stainless steel sheet cathode. The electrolyte contained 125 ml. hydrofluosilicic acid (30% by weight H SiF and 25 ml. ethylene glycol. An anodic current density of approximately 1000 a.s.f. was applied for about 40 seconds with a current of 200 milliamperes. The total exposed area of a 36 bit word line is approximately 0.03 square inch. The electrolyte temperature was maintained at from 20 to 30 C. Satisfactory etching of the necks was achieved without corrosion cracking of adjacent bit areas.
- a method for smoothly etching the surface of a Be-Cu alloy part containing grains of cobalt beryllide comprising anodically etching said part in an electrolyte of the following composition:
- hydrofiuosilicic acid a major portion of hydrofiuosilicic acid, as 30% by HgSiFs,
- An electrolyte composition for smoothly etching a Be-Cu alloy part containing cobalt beryllide grains when said part is immersed as an anode in said electrolyte comprising:
- hydrofluosilicic acid a major portion of hydrofluosilicic acid, as 30% by weight H SiF a minor portion of ethylene glycol,
- Hydrofluosilicic acid as 30% by weight aqueous H SiF ml 60 Hydroxylamine hydrochloride gm 0.5 Ethylene glycol ml 20 Isopropyl alcohol containing dissolved therein 0.2
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
- Weting (AREA)
- ing And Chemical Polishing (AREA)
Description
United States Patent 3,445,355 METHOD AND COMPOSITION FOR THE ELEC TROLYTIC ETCHING OF BERYLLIUM-COPPER ALLOYS Paul T. Woodberry, Reading, Mass., and Herman Koretzky, Poughkeepsie, N.Y., assignors to International Business Machines Corporation, Armonk, N.Y., a corporation of New York No Drawing. Filed July 15, 1966, Ser. No. 565,386
Int. Cl. C23b 3/02 US. Cl. 204-141 9 Claims The present invention relates to a method and electrolyte composition for electrolytically etching metal alloys. In particular, the invention is concerned with the electrolytic etching of beryllium-copper alloys, especially beryllium-copper alloys containing cobalt in the form of cobalt-beryllide.
Many beryllium-copper alloys contain cobalt. When such alloys are precipitation-hardened, grains of the intermetallic compound cobalt beryllide are formed in a matrix of copper. The resulting two-phased system is difiicult to smooth or polish by conventional electrolytic etching techniques. The major diificulty is that the anodic potentials established at the surfaces of the two phases result in a preferential dissolution of one of the phases. The other phase protrudes at surfaces and edges and this results in a rough surface, rather than the desired smooth surface.
Accordingly, the objective of the present invention is to provide an electrolyte composition and method for smoothly etching beryllium-copper alloys, especially beryllium-copper alloys containing cobalt beryllide.
A further specific objective of the invention is to provide a composition and method for electrolytically smoothing beryllium-copper alloys containing grains of copper beryllide.
The manner in which the above objectives and many other highly desirable objects and advantages are achieved in accordance with the present invention will be apparent in view of the following detailed description of preferred embodiments thereof.
In general, the present invention comprises anodically etching an article of a beryllium-copper alloy containing cobalt-beryllide grains to provide a smooth surface on the article by connecting the article as anode in an electrolytic system including an electrolyte containing the following constituents:
hydrofiuosilicic acid, H SiF ethylene glycol, hydroxylamine hydrochloride, isopropyl alcohol, and
2,2 diquinoline.
Hydrofluosilicic acid, considering, for example, a bath of about 105 ml. volume, comprises the major portion by volume of the composition, generally over 50% and usually on the order of about 60% by volume. The hydrofiuosilicic acid is used as 30% by weight aqueous H SiF Ethylene glycol is present in a substantial but minor proportion, generally on the order of about 20% by volume of the composition. The hydroxylamine hydrochloride is present in a small amount, generally on the order of 1 gm. and preferably about 0.5 gm. The 2,2 diquinoline also is present in a small amount, usually less than 1 gm. and preferably about 0.2 gm. and is dissolved in the isopropyl alcohol. The isopropyl alcohol is present in minor proportions which may comprise about 20% by volume of the composition.
The anodic current density on the surface of the part etched with this composition is preferably in the range "ice of from about 500 to 1000 amperes per square foot (a.s.f.).
The invention will be more fully appreciated in the light of the following example which illustrates a preferred embodiment of the composition.
EXAMPLE 1 A part of beryllium-copper alloy which has been precipitation-hardened to form grains of cobalt-beryllide in a matrix of copper was anodically connected in an electrolytic cell which also included a stainless steel cathode plate opposite the part. An electrolyte of the following formulation was introduced into the cell:
about 30 C. and a current density of 500 a.s.f. was applied for 30 seconds. The pH of the electrolyte was maintained between 4 and 5. A smooth surface was produced on the metal part.
The distribution of current over the surface of the part electrolytically etched can be adjusted to effect overall uniform attack. This is accomplished by the use of shaped cathodes, current shields and current thieves. Addition agents can be included in the bath formulation to alter electrical conductivity and solution viscosity as well as the composition of the film at the anode surfaces. The above factors are determined experimentally for each system and part configuration.
An electrolyte comprising a major portion of hydrofluosilicic acid and a minor portion of ethylene glycol, not including the other above-described additives, has also been found to be useful for through-etching of Be-Cu alloys and for etching Ni-Fe-P magnetic alloy films.
Beryllium-copper alloys have been found to be useful in the production of substrates for electrical components. In one application, the metal sheets are suitably masked and etched through their entire thicknesses to form chainlike structures. Generally, the conventional process for accomplishing the etching has involved exposure to aqueous chemical solutions, such as acidified ferric chloride or ammonium persulfate. The rate of dissolution, however, in such chemical etchants is influenced by the concentration of the solution, the presence of dissolved copper salts, and the temperature of the solution, as well as the degree of agitation of the solution. Thus, in the same period of time, one part may be etched properly and another part over-etched or under-etched due to slight variation in conditions.
Where the part to be etched is a piece of berylliumcopper alloy which is to be etched completely through at one or more points, the part is first provided with a coating of a suitable masking or resist material to confine the etching to the desired portions of the base metal. The part is then positioned between two cathodes which may be copper or stainless steel sheets and is connected as the anode in the system. The electrolyte is then introduced into the cell and an anodic current density of at least 50 a.s.f. is applied.
Where the part to be etched is nickel-iron-phosphorus alloy, the preferred electrolyte is an aqueous solution of hydrofiuosilicic acid and ethylene glycol. For this embodiment, the preferred cathode material is stainless steel sheet or foil and the anodic current density on the part is preferably in the range of from 500 to 2000 a.s.f.
The following two examples, Examples 2 and 3, illustrate the above-described electrolytic etching of Be-Cu and Ni-Fe-P alloys.
EXAMPLE 2 A piece of beryllium-copper alloy 0.003 inch thick is anodically connected between two stainless steel cathodes. The sheet is provided with resist coated areas on those portions of the surface which are not be to etched. An anodic current density of 500 a.s.f. is applied to the part for two minutes in an electrolyte comprising 125 ml. (30% by weight of H SiF and 25 ml. of reagent grade ethylene glycol.
There is no substantial attack on the beryllium-copper alloy in the absence of passage of the direct current through the part.
The extent and rate of removal of the base metal is not influenced by small changes in solution temperature. The amount of metal removal can be ascertained and controlled through the use of Ampere-hour meters. The rate of penetration is directly related to the current density selected.
EXAMPLE 3 A thin film of nickel-iron-phosphorus magnetic alloy was deposited on a palladium coated beryllium-copper alloy. Magnetic alloy bits, in a density of 36 bits to a word line, were protected with a resist material. The necks between the covered or protected bits were then etched by immersing the part as an anode in an electrolytic cell containing a stainless steel sheet cathode. The electrolyte contained 125 ml. hydrofluosilicic acid (30% by weight H SiF and 25 ml. ethylene glycol. An anodic current density of approximately 1000 a.s.f. was applied for about 40 seconds with a current of 200 milliamperes. The total exposed area of a 36 bit word line is approximately 0.03 square inch. The electrolyte temperature was maintained at from 20 to 30 C. Satisfactory etching of the necks was achieved without corrosion cracking of adjacent bit areas.
It will be apparent to those skilled in the art that various changes may be made in the compositions and procedures described above without departing from the spirit or scope of the invention as expressed in the following claims.
What is claimed is:
1. A method for smoothly etching the surface of a Be-Cu alloy part containing grains of cobalt beryllide comprising anodically etching said part in an electrolyte of the following composition:
a major portion of hydrofiuosilicic acid, as 30% by HgSiFs,
a minor portion of ethylene glycol,
a small amount of hydroxylamine hydrochloride, and
a minor portion of isopropyl alcohol containing dissolved therein a small amount of 2,2 diquinoline.
Hydrofluosilicic acid as 30% by weight H SiF ml Hydroxylamine hydrochloride grn 0.5
Ethylene glycol ml 20 Isopropyl alcohol containing dissolved therein 0.2
gm, 2,2 diquinoline ml 25 4. The method of claim 1 wherein a current density of from 500 to 1000 a.s.f. is applied to the surface of said part.
5. An electrolyte composition for smoothly etching a Be-Cu alloy part containing cobalt beryllide grains when said part is immersed as an anode in said electrolyte comprising:
a major portion of hydrofluosilicic acid, as 30% by weight H SiF a minor portion of ethylene glycol,
a minor portion of isopropyl alcohol having dissolved therein a small amount of 2,2 diquinoline, and
a small amount of hydroxylamine hydrochloride.
6. An electrolyte as described in claim 5 wherein said hydrofluosilicic acid is on the order of about 60% by volume of said composition, said ethylene glycol is on the order of about 20% and said isopropyl alcohol is on the order of about 20% by volume.
7. An electrolyte as described in claim 5 having the following composition:
Hydrofluosilicic acid as 30% by weight aqueous H SiF ml 60 Hydroxylamine hydrochloride gm 0.5 Ethylene glycol ml 20 Isopropyl alcohol containing dissolved therein 0.2
gm. 2,2 diquinoline ml 25 References Cited UNITED STATES PATENTS 2/1937 Donahue -150 3/1940 Gahaean 75-150 ROBERT K. MIHALEK, Primary Examiner.
Claims (2)
1. A METHOD FOR SMOOTHLY ETCHING THE SURFACE OF A BE-CU ALLOY PART CONTAINING GRAINS OF COBALT BERYLIDE COMPRISING ANODICALLY ETCHING SAID PART IN AN ELECTROLYTE OF THE FOLLOWING COMPOSITION: A MAJOR PORTION OF HYDROFLUOSILICIC ACID, AS 30% BY WEIGHT H2SIF6, A MINOR PORTION OF ETHYLENE GLYCOL, A SMALL AMOUNT OF HYDROXYLAMINE HYDROCHLORIDE, AND A MINOR PORTION OF ISOPROPYL ALCOHOL CONTAINING DISSOLVED THEREIN A SMALL AMOUNT OF 2,2'' DIQUINOLINE.
5. AN ELECTROLYTE COMPOSITION FOR SMOOTHLY ETCHING A BE-CU ALLOY PART CONTAINING COBALT BERYLLIDE GRAINS WHEN SAID PART IS IMMERSED AS AN ANODE IN SAID ELECTROLYTE COMPRISING: A MAJOR PORTION OF HYDROFLUOSILICIC ACID, AS 30% BY WEIGHT H2SIF6, A MINOR PORTION OF ETHYLENE GLYCOL, A MINOR PORTION OF ISOPROPYL ALCOHOL HAVING DISSOLVED THEREIN A SMALL AMOUNT OF 2,2'' DIQUINOLINE, AND A SMALL AMOUNT OF HYDROXYLAMINE HYDROCHLORIDE.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US56538666A | 1966-07-15 | 1966-07-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3445355A true US3445355A (en) | 1969-05-20 |
Family
ID=24258378
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US565386A Expired - Lifetime US3445355A (en) | 1966-07-15 | 1966-07-15 | Method and composition for the electrolytic etching of beryllium-copper alloys |
Country Status (5)
Country | Link |
---|---|
US (1) | US3445355A (en) |
JP (1) | JPS4932690B1 (en) |
DE (1) | DE1621090A1 (en) |
FR (1) | FR1527508A (en) |
GB (1) | GB1166901A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3663386A (en) * | 1971-02-08 | 1972-05-16 | Basf Wyandotte Corp | Electrocleaner composition and process |
US4169027A (en) * | 1977-07-05 | 1979-09-25 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method of electrochemically processing the surface of a workpiece of molybdenum or of an alloy containing a high proportion of molybdenum |
US20110272287A1 (en) * | 2010-05-07 | 2011-11-10 | International Business Machines Corporation | Method for patterning magnetic films |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3400249A1 (en) * | 1984-01-05 | 1985-07-18 | Hoechst Ag, 6230 Frankfurt | METHOD FOR ELECTROCHEMICALLY Roughening ALUMINUM FOR PRINTING PLATE CARRIERS IN AN AQUEOUS MIXED ELECTROLYTE |
DE3400250A1 (en) * | 1984-01-05 | 1985-07-18 | Hoechst Ag, 6230 Frankfurt | METHOD FOR ELECTROCHEMICALLY Roughening ALUMINUM FOR PRINTING PLATE CARRIERS IN AN AQUEOUS MIXED ELECTROLYTE |
DE3400248A1 (en) * | 1984-01-05 | 1985-07-18 | Hoechst Ag, 6230 Frankfurt | METHOD FOR ELECTROCHEMICALLY Roughening ALUMINUM FOR PRINTING PLATE CARRIERS IN AN AQUEOUS MIXED ELECTROLYTE |
RU2664994C1 (en) * | 2017-11-15 | 2018-08-24 | Российская Федерация, от имени которой выступает Министерство промышленности и торговли Российской Федерации (Минпромторг России) | Electrolyte for electrolyte-plasma polishing of parts made of refractory alloys |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2072067A (en) * | 1934-01-29 | 1937-02-23 | Feldspathic Res Corp | Method of preparing beryllium alloys |
US2193482A (en) * | 1938-11-14 | 1940-03-12 | Beryllium Corp | Process for the production of alloys of beryllium and copper |
-
1966
- 1966-07-15 US US565386A patent/US3445355A/en not_active Expired - Lifetime
-
1967
- 1967-06-08 JP JP42036273A patent/JPS4932690B1/ja active Pending
- 1967-06-12 FR FR8548A patent/FR1527508A/en not_active Expired
- 1967-06-26 GB GB29309/67A patent/GB1166901A/en not_active Expired
- 1967-07-10 DE DE19671621090 patent/DE1621090A1/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2072067A (en) * | 1934-01-29 | 1937-02-23 | Feldspathic Res Corp | Method of preparing beryllium alloys |
US2193482A (en) * | 1938-11-14 | 1940-03-12 | Beryllium Corp | Process for the production of alloys of beryllium and copper |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3663386A (en) * | 1971-02-08 | 1972-05-16 | Basf Wyandotte Corp | Electrocleaner composition and process |
US4169027A (en) * | 1977-07-05 | 1979-09-25 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method of electrochemically processing the surface of a workpiece of molybdenum or of an alloy containing a high proportion of molybdenum |
US20110272287A1 (en) * | 2010-05-07 | 2011-11-10 | International Business Machines Corporation | Method for patterning magnetic films |
Also Published As
Publication number | Publication date |
---|---|
JPS4932690B1 (en) | 1974-09-02 |
FR1527508A (en) | 1968-05-31 |
DE1621090A1 (en) | 1971-04-22 |
GB1166901A (en) | 1969-10-15 |
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