US3637468A - Electrodes for electrolytic processes - Google Patents
Electrodes for electrolytic processes Download PDFInfo
- Publication number
- US3637468A US3637468A US819142A US3637468DA US3637468A US 3637468 A US3637468 A US 3637468A US 819142 A US819142 A US 819142A US 3637468D A US3637468D A US 3637468DA US 3637468 A US3637468 A US 3637468A
- Authority
- US
- United States
- Prior art keywords
- electrode
- carbon
- layer
- electrode assembly
- electrolyte
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title abstract description 18
- 230000008569 process Effects 0.000 title abstract description 18
- 230000002745 absorbent Effects 0.000 claims abstract description 33
- 239000002250 absorbent Substances 0.000 claims abstract description 33
- 239000003792 electrolyte Substances 0.000 claims description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 229910052799 carbon Inorganic materials 0.000 claims description 17
- 238000011282 treatment Methods 0.000 claims description 7
- 238000009826 distribution Methods 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 5
- 239000004568 cement Substances 0.000 claims description 3
- 239000011810 insulating material Substances 0.000 claims description 3
- 239000012811 non-conductive material Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 25
- 239000003575 carbonaceous material Substances 0.000 abstract description 22
- 238000009713 electroplating Methods 0.000 abstract description 3
- 230000005684 electric field Effects 0.000 description 8
- 238000007747 plating Methods 0.000 description 8
- 238000003754 machining Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000005498 polishing Methods 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 238000004070 electrodeposition Methods 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 229910002804 graphite Inorganic materials 0.000 description 3
- 239000010439 graphite Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 150000002739 metals Chemical group 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000000712 assembly Effects 0.000 description 2
- 238000000429 assembly Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012809 cooling fluid Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 101100264195 Caenorhabditis elegans app-1 gene Proteins 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910003481 amorphous carbon Inorganic materials 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004758 synthetic textile Substances 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
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/10—Electrodes, e.g. composition, counter electrode
- C25D17/14—Electrodes, e.g. composition, counter electrode for pad-plating
-
- 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
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S204/00—Chemistry: electrical and wave energy
- Y10S204/07—Current distribution within the bath
Definitions
- the absorbent material that is conventionally used, for example, in the brush or tampon process, consists of an absorbent porous carbon material.
- a device for use in this context can comprise an electrode in contact with at least one carbon material member.
- Electrolytic processes using brush and tampon, etc. are well known and have important industrial applications, not only in the fields of metal and metal-alloy depositions but also in the field of electrochemical treatments and applications, such as for example: anodic oxidation, electrochemical machining and/or polishing, etc.
- the characteristics are much the same whether the workpiece to be treated be the cathode or the anode.
- the process consists essentially in moving an absorbent device, impregnated with an appropriate electrolyte, on the conductive workpiece to be treated.
- the invention consists in an electrolytic process utilizing highly absorbent porous carbon materials, particularly in those processes known as brush or tampon processes, and is applicable both to anodic systems, e.g., for the deposition of metals, and to cathodic systems, e.g., for anodic oxidation, electrochemical machining and electrolytic polishing.
- the invention also consists in a device useful to carry out this process, and comprising an electrode in contact with at least one carbon material member.
- the member is preferably nonrigid and may be cemented to the electrode with organic substances followed or not by pyrolysis. Alternatively, the parts may be attached to one another by threads which may or may not be, carbon.
- Electrodes may be used in contact with electrodes, to receive electrolytic feeding; to serve as devices for the circulation of a fluid; to enable them to be heated by the same means or by an electric current, or to be polarized in relation to the electrode. They may also be used in electrolysis by means of fused salts. In tank plating processes they may be used to change the behavior of soluble anodes or to establish an homogeneous electric field or to improve electrodes used in electrochemical machining.
- FIG. 1 shows a diagrammatic representation of the known electrodeposition of metals
- FIG. 2 schematically shows a known system of electrolytic plating with cooling
- FIG. 3 shows a first embodiment of a device according to the invention
- FIG. 4 shows how the distance between a pseudoanode and a cathode can remain constant
- FIG. 5 shows an anode with certain fittings
- FIG. 6 shows an insulating component
- FIG. 7 shows a means for the distribution of electrolytes
- FIG. 8 shows a device capable of receiving electrolysis of fused salts
- FIG. 9 shows a device comprising a protecting ring
- FIG. 10 shows a cross section along the line X-X of FIG. 9, and
- FIG. 11 schematically shows how a substantially uniform electric field is obtained.
- FIG. 1 shows an anode 1 in contact with an absorbent material 2 that is rendered electrically conductive by impregnating it with an appropriate electrolyte, the constituent materials of the tampon being preferably hydrophilous cotton-wool, cellulose, etc., or hydrophobic synthetic fabrics, brushes with nonconductive bristles, etc., or a combination of these.
- the whole of the anode l and the absorbent material 2 is contained in an electrically nonconductive head T.
- the anode 1 and a workpiece 3 to be plated forming the cathode are, of course, connected to an electric power source schematically illustrated at G.
- This device may use either soluble anodes (e.g., copper in the case of electrodeposition of copper), or alternatively nonsoluble anodes.
- FIG. 2 represents schematically the plating of a rotating, cylindricalshaped workpiece component 3, a water jacket in which the cooling fluid 5 circulates being incorporated in the anode 1.
- the thickness of the latter is to be as thin as possible (see example in FIG. 2).
- the absorbent power of this material is therefore reduced and the circulation of the electrolyte which occasionally is injected, consequently becomes more difficult.
- FIG. 3 shows a device which illustrates in principle the object of the present invention.
- the anode 1 is put into contact with a porous carbon material member C2 placed in between the anode l and the nonconductive absorbent material 2.
- These carbon materials may absorb for example an amount of electrolyte equal to percent of their proper volume. Considering that their own electric conductivity is far superior to that of the impregnating electrolyte, for example about 90 percent of the current passing through the device may thus be conducted by this porous material. Consequently, one may use a voluminous absorbent material C2 and 2.
- the thickness of the nonconductive absorbent material 2 may be reduced since the carbonaceous material C2 serves as an anode and is therefore in close contact with the surface of the workpiece 3 to be treated. For this reason the electric field is much more homogeneous, the coating more even, the Joule effect reduced, all of which represents an important advantage.
- this absorbent material is nonrigid and adaptable to any complex shaped profiles without requiring any specific machining of the anode 1; since the easily adaptable, conductive carbonaceous absorbent part operates as an anode, the distance between this pseudoanode and the cathode remains constant (FIG. 4).
- the intrinsic electrical conductivity of the material of the member C2 makes it easy to provide the anode l with different fittings e.g., perforated electrolyte tubes 6 made of insulating materials 7 as shown in FIG. 5; mechanically or otherwise deformable anodes, even by an insulating component 8 as shown in FIG. 6, since the electric current is distributed by the carbonaceous material C2 underneath this insulator and therefore maintains a uniform electric field without any blanketing effect.
- porous carbon materials are very suitable for the manufacture of complicated assemblies.
- organic cements they may be attached together or to carbon or graphite supports or other materials with a basic carbon content.
- the assemblies thus obtained may subsequently be heat treated, i.e., pyrogenized or pyrolyzed as a result of which an entirely carbonaceous matter is obtained.
- the chemical inertia of the absorbent carbon materials allows for the use of electrolytes such as those containing concentrated sulphuric or phosphoric base acid which normally cannot be used with nonpyrolyzed absorbent organic materials.
- the device of FIG. 7 can be adapted for electrolytic polishing, the workpiece 3 becoming the anode and the electrode 1 becoming the cathode.
- FIG. 9 shows a device comprising a protecting ring C23.
- This ring is made of a graphite tube 14 fixed and pyrogenated onto a ring C23 of porous carbon material and is subsequently polarized in relation to the anode l by an auxiliary power source GA for example.
- the protecting ring is insulated by an insulating liner 15 from the porous absorbent material C2 in contact with the anode 1 and is placed inside the noncarbonaceous absorbent mass 2.
- FIG. 10 shows a cross section along the line X-X of FIG. 9 of the different components of this protecting ring C23.
- Insoluble anodes are often sensitive to electrolytic reaction and are subject to wear in the long run.
- the use of conductive absorbent material acting more or less as an anode as shown in FIG. 3 protects the insoluble anodes from this type of wear.
- An accidental short circuit between the carbonaceous material and the workpiece is temporary and without danger since the contact, being perfectly wet, prevents sudden current rises.
- the material reduces the dissolution of the anode, for example: with an appropriate thickness of the carbonaceous material the rate of dissolution of the anode may be kept equal to the rate of deposition on the cathode in case the latter is inferior to the former.
- anodes clad with one of these materials that may also serve as a filter for the residues from the anode dissolution, maintain the stability of the bath plating solutions.
- the porous carbon material 17 close to the cathode 16 a uniform electric field is achieved and provided that its thickness is small the material does not act as an intermediate electrode since due to its porous texture any metallic deposit is avoided as shown in FIG. 11.
- cathodes modified according to the present invention represent a considerable advantage.
- electrochemical machining consists essentially in an electrolytic attack of the anodic part with a suitable electrolyte by means of an insoluble cathode having a shape similar to that of the part to be machined.
- a very small gap between anode and cathode (approx. 20/100 mm. in most cases) is absolutely necessary to ensure an electric field as uniform as possible and to allow the highest current densities, a rapidly flowing electrolyte being passed into the gap. Since the cross section of the electrolyte flow is very small, the electrolyte must be injected under high pressure requiring strong supports able to resist heavy mechanical stresses and to ensure a precise positioning of the anode and cathode.
- a cathode clad with a porous amorphous or graphitized carbon material due to its permeability during the electrolyte flow (e.g., 90 percent of its proper volume) makes it possible to increase considerably the speed of the electrolyte flow (e.g., 200 times) and to reduce in an even greater proportion the pressure required for the electrolyte circulation while still maintaining a very small gap owing to the fact that the porous carbon material acts partially or totally as an electrode due to its very high electric conduc tivity. Consequently, it is easier to provide the supports and it is even possible to operate in open tanks as used for conventional electrolytic treatments, thus reducing the danger of explosive gas mixtures, the detrimental rise or variation of temperature, the danger of accidental short circuits, etc.
- FIGS. 5, 6, 7 and 9 are also applicable for electrodes used for electrochemical machining without tampons as well as for other electrochemical treatments in tanks where such type of electrodes provide a solution to the high current density conditions and forced electrolyte circulation.
- a process for the electrolytic treatment of a conductive workpiece wherein said workpiece is held in contact with one face of a constant thickness layer of a nonconductive absorbent material, the opposite face of said layer is held in contact with one face of a layer of highly absorbent flexible electrically conductive material of fibrous porous carbon permanently filled with electrolyte, the opposite face of said carbon layer is held in contact with a conductive electrode element, the workpiece is connected to one pole of an electrical power source, and the electrode element is connected to the other pole of said power source.
- An electrode assembly for the electrolytic treatment of a conductive workpiece comprising an electrode layer element connectable to one terminal of an electrical power source, an electrically conductive layer of a highly absorbent flexible fibrous carbon in contact with said electrode layer, and a layer of porous nonconductive material in contact over one face thereof with said carbon layer and adapted, while remaining of constant thickness, to be held with its opposite face in contact with the workpiece which is to be treated and which is connectable to the other terminal of said power source.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electroplating Methods And Accessories (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR149897 | 1968-04-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
US3637468A true US3637468A (en) | 1972-01-25 |
Family
ID=8649557
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US819142A Expired - Lifetime US3637468A (en) | 1968-04-29 | 1969-04-25 | Electrodes for electrolytic processes |
Country Status (11)
Country | Link |
---|---|
US (1) | US3637468A (xx) |
BE (1) | BE731512A (xx) |
CH (1) | CH514352A (xx) |
DE (1) | DE1921274B2 (xx) |
ES (1) | ES366577A1 (xx) |
FR (1) | FR1585605A (xx) |
GB (1) | GB1264871A (xx) |
LU (1) | LU58475A1 (xx) |
NL (1) | NL143619B (xx) |
NO (1) | NO128432B (xx) |
SE (1) | SE356536B (xx) |
Cited By (45)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3974050A (en) * | 1971-10-12 | 1976-08-10 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method of and apparatus for processing the surface of bodies |
JPS524440A (en) * | 1975-06-18 | 1977-01-13 | Toshio Moriyama | Electrolytic pigmentation process for stainless steel |
US4043891A (en) * | 1976-01-14 | 1977-08-23 | Bell Telephone Laboratories, Incorporated | Electrolytic cell with bipolar electrodes |
US4073714A (en) * | 1975-04-10 | 1978-02-14 | Norsk Hydro A.S | Means for cooling of self-baking anodes in aluminum electrolysis cells |
US4202739A (en) * | 1977-04-25 | 1980-05-13 | The United States of America as represented by the United Stated Department of Energy | Electrochemical removal of material from metallic work |
US4287045A (en) * | 1978-11-10 | 1981-09-01 | Institut De Recherches De La Siderurgie Francaise | Cooled electrode adapted to contact molten metal |
US4360417A (en) * | 1980-07-03 | 1982-11-23 | Celanese Corporation | Dimensionally stable high surface area anode comprising graphitic carbon fibers |
US4431501A (en) * | 1980-08-05 | 1984-02-14 | Outokumpu Oy | Apparatus for electrolytic polishing |
US4650549A (en) * | 1985-11-06 | 1987-03-17 | Hughes Tool Company | Method for electroplating helical rotors |
US4668364A (en) * | 1986-05-21 | 1987-05-26 | Farmer Fred W | Portable electroplating apparatus |
DE3630919A1 (de) * | 1986-09-11 | 1988-04-07 | Harald Haffke | Handgeraet zur verzinkung metallischer oberflaechen, insbesonders von karosserien mit hilfe der galvanotechnik ueber eine fahrzeug-stromquelle |
US4776933A (en) * | 1986-04-25 | 1988-10-11 | Poligrat Gmbh | Electrochemical polishing and pickling method and apparatus |
US4786389A (en) * | 1987-09-25 | 1988-11-22 | Amp Incorporated | Electroplating apparatus |
US4806216A (en) * | 1988-01-21 | 1989-02-21 | The United States Of America As Represented By The United States Department Of Energy | Electrochemical polishing of notches |
US4874496A (en) * | 1989-01-06 | 1989-10-17 | Maryan Chak | Device for silverizing drinking water |
US4944856A (en) * | 1989-04-19 | 1990-07-31 | Westinghouse Electric Corp. | Electrolytic etching apparatus and method for marking metal tubes with sequential identification numbers |
US4992154A (en) * | 1988-08-19 | 1991-02-12 | Marui Mekki Kogyo Yugen Kaisha | Brush for electrolytic treatment |
US5207882A (en) * | 1990-12-05 | 1993-05-04 | Saulius Baublys | Apparatus for electrochemical marking of workpieces |
US5225059A (en) * | 1992-08-03 | 1993-07-06 | W. R. Associates | Apparatus for single anode brush electroplating |
US5322613A (en) * | 1992-11-23 | 1994-06-21 | Tomy K.K. | Method and apparatus for marking orthodontic products |
US5401369A (en) * | 1994-01-21 | 1995-03-28 | Gershin; Mircea-Mike | Electroplating pen |
US5409593A (en) * | 1993-12-03 | 1995-04-25 | Sifco Industries, Inc. | Method and apparatus for selective electroplating using soluble anodes |
FR2767340A1 (fr) * | 1997-08-13 | 1999-02-19 | Dalic Selective Plating Gmbh | Procede pour combler des pores et/ou des microfissures presents a la surface d'un substrat en metal oxydable |
FR2821627A1 (fr) * | 2001-03-05 | 2002-09-06 | Lorilleux | Procede et dispositif d'elaboration par voie electrolytique d'un depot selectif epais de nickel sur une piece |
US20030094364A1 (en) * | 1998-12-01 | 2003-05-22 | Homayoun Talieh | Method and apparatus for electro-chemical mechanical deposition |
US20040244910A1 (en) * | 2001-06-14 | 2004-12-09 | Anton Albrecht | Method and device for locally removing coating from parts |
US6843904B1 (en) * | 1999-10-21 | 2005-01-18 | Matsushita Electric Industrial Co., Ltd. | Inspection and repair of active type substrate |
US20050016868A1 (en) * | 1998-12-01 | 2005-01-27 | Asm Nutool, Inc. | Electrochemical mechanical planarization process and apparatus |
US20060006073A1 (en) * | 2004-02-27 | 2006-01-12 | Basol Bulent M | System and method for electrochemical mechanical polishing |
US20060070885A1 (en) * | 1999-09-17 | 2006-04-06 | Uzoh Cyprian E | Chip interconnect and packaging deposition methods and structures |
US20070042129A1 (en) * | 2005-08-22 | 2007-02-22 | Kang Gary Y | Embossing assembly and methods of preparation |
US20070051635A1 (en) * | 2000-08-10 | 2007-03-08 | Basol Bulent M | Plating apparatus and method for controlling conductor deposition on predetermined portions of a wafer |
US20070128851A1 (en) * | 2001-01-05 | 2007-06-07 | Novellus Systems, Inc. | Fabrication of semiconductor interconnect structures |
US20080169204A1 (en) * | 2006-10-25 | 2008-07-17 | Rolls-Royce Plc | Method and apparatus for treating a component of a gas turbine engine |
US20080237048A1 (en) * | 2007-03-30 | 2008-10-02 | Ismail Emesh | Method and apparatus for selective electrofilling of through-wafer vias |
US20080304975A1 (en) * | 2007-06-05 | 2008-12-11 | Rolls-Royce Plc | Method for producing abrasive tips for gas turbine blades |
US20090280243A1 (en) * | 2006-07-21 | 2009-11-12 | Novellus Systems, Inc. | Photoresist-free metal deposition |
US20100150730A1 (en) * | 2008-12-15 | 2010-06-17 | Rolls-Royce Plc | Component having an abrasive layer and a method of applying an abrasive layer on a component |
US20100193362A1 (en) * | 2007-05-09 | 2010-08-05 | Terunori Warabisako | Method for processing silicon base material, article processed by the method, and processing apparatus |
US20100224501A1 (en) * | 2000-08-10 | 2010-09-09 | Novellus Systems, Inc. | Plating methods for low aspect ratio cavities |
US20110054397A1 (en) * | 2006-03-31 | 2011-03-03 | Menot Sebastien | Medical liquid injection device |
WO2013064616A3 (en) * | 2011-11-04 | 2014-07-31 | Integran Technologies | Flow-through consumable anodes |
US20170253988A1 (en) * | 2016-03-01 | 2017-09-07 | The Boeing Company | Electromodification of Conductive Surfaces |
US10526717B2 (en) | 2015-02-27 | 2020-01-07 | Biomet Uk Healthcare Limited | Apparatus and method for selectively treating a surface of a component |
US20220186396A1 (en) * | 2020-12-11 | 2022-06-16 | Metaly S.R.L. | Equipment for oxidation of planar metallic surfaces, such as sheet, fabric or metal net and method of application of the treatment |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI834686A0 (fi) * | 1983-12-20 | 1983-12-20 | Niinivaara Ensi Kyoesti Juhani | Foerfarande foer undervattensrening och -belaeggning |
Citations (5)
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GB190018643A (en) * | 1900-10-18 | 1901-08-17 | Thomas Grant | Improvements in Single Cylinder Compound Compressors |
GB493108A (en) * | 1937-03-31 | 1938-09-30 | Alfred Reginald Thomas | Improvements in or relating to the electro-deposition of metals |
US3346477A (en) * | 1964-06-08 | 1967-10-10 | W & W Products | Hand instrument for electrolytic and acid etching |
US3471383A (en) * | 1965-02-05 | 1969-10-07 | Gaf Corp | Continuous anode for electrolytic cells |
US3474013A (en) * | 1965-07-17 | 1969-10-21 | Inoue K | Method of and apparatus for the electrochemical machining of a conductive workpiece |
-
1968
- 1968-04-29 FR FR149897A patent/FR1585605A/fr not_active Expired
-
1969
- 1969-04-15 BE BE731512D patent/BE731512A/xx not_active IP Right Cessation
- 1969-04-22 CH CH608469A patent/CH514352A/fr not_active IP Right Cessation
- 1969-04-24 LU LU58475D patent/LU58475A1/xx unknown
- 1969-04-25 US US819142A patent/US3637468A/en not_active Expired - Lifetime
- 1969-04-25 GB GB1264871D patent/GB1264871A/en not_active Expired
- 1969-04-25 DE DE19691921274 patent/DE1921274B2/de not_active Withdrawn
- 1969-04-28 SE SE06031/69A patent/SE356536B/xx unknown
- 1969-04-28 NO NO691768A patent/NO128432B/no unknown
- 1969-04-29 ES ES366577A patent/ES366577A1/es not_active Expired
- 1969-04-29 NL NL696906587A patent/NL143619B/xx not_active IP Right Cessation
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB190018643A (en) * | 1900-10-18 | 1901-08-17 | Thomas Grant | Improvements in Single Cylinder Compound Compressors |
GB493108A (en) * | 1937-03-31 | 1938-09-30 | Alfred Reginald Thomas | Improvements in or relating to the electro-deposition of metals |
US3346477A (en) * | 1964-06-08 | 1967-10-10 | W & W Products | Hand instrument for electrolytic and acid etching |
US3471383A (en) * | 1965-02-05 | 1969-10-07 | Gaf Corp | Continuous anode for electrolytic cells |
US3474013A (en) * | 1965-07-17 | 1969-10-21 | Inoue K | Method of and apparatus for the electrochemical machining of a conductive workpiece |
Cited By (60)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3974050A (en) * | 1971-10-12 | 1976-08-10 | Kernforschungsanlage Julich Gesellschaft Mit Beschrankter Haftung | Method of and apparatus for processing the surface of bodies |
US4073714A (en) * | 1975-04-10 | 1978-02-14 | Norsk Hydro A.S | Means for cooling of self-baking anodes in aluminum electrolysis cells |
JPS524440A (en) * | 1975-06-18 | 1977-01-13 | Toshio Moriyama | Electrolytic pigmentation process for stainless steel |
US4043891A (en) * | 1976-01-14 | 1977-08-23 | Bell Telephone Laboratories, Incorporated | Electrolytic cell with bipolar electrodes |
US4202739A (en) * | 1977-04-25 | 1980-05-13 | The United States of America as represented by the United Stated Department of Energy | Electrochemical removal of material from metallic work |
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Also Published As
Publication number | Publication date |
---|---|
NO128432B (xx) | 1973-11-19 |
FR1585605A (xx) | 1970-01-30 |
NL143619B (nl) | 1974-10-15 |
LU58475A1 (xx) | 1969-07-22 |
NL6906587A (xx) | 1969-10-31 |
CH514352A (fr) | 1971-10-31 |
GB1264871A (xx) | 1972-02-23 |
BE731512A (xx) | 1969-09-15 |
DE1921274B2 (de) | 1971-11-11 |
DE1921274A1 (de) | 1969-11-06 |
SE356536B (xx) | 1973-05-28 |
ES366577A1 (es) | 1971-03-16 |
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