US20080135135A1 - Method For Treating Metallic Surfaces With an Alternating Electrical Current - Google Patents
Method For Treating Metallic Surfaces With an Alternating Electrical Current Download PDFInfo
- Publication number
- US20080135135A1 US20080135135A1 US11/953,441 US95344107A US2008135135A1 US 20080135135 A1 US20080135135 A1 US 20080135135A1 US 95344107 A US95344107 A US 95344107A US 2008135135 A1 US2008135135 A1 US 2008135135A1
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- United States
- Prior art keywords
- zinc
- metallic surface
- silicate
- amps
- medium
- 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.)
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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
- C25D9/00—Electrolytic coating other than with metals
- C25D9/04—Electrolytic coating other than with metals with inorganic materials
Definitions
- Prior art processes have employed electrolytic cathodic process to deposit a beneficial layer with improved corrosion resistance on zinc, zinc alloy plated substrates and zinc diecast components.
- First the deposition of Silicon is not inherently cathodic in nature. Therefore, without wishing to be bound by any theory or explanation, it is believed that the resulting layer is the result of the pH environment created by the cathodic polarity of the surface, not the direct reduction on the surface due to the availability of electrons.
- a companion reaction which occurs at the anode. This companion reaction may facilitate the beneficial result and in typical Zinc plating where the Zinc+ ions required for plating can be electrically oxidized at the anode for electro-reduction to zinc metal at the cathode.
- an electrolytic process for treating a metallic surface with silicates in order to improve the corrosion resistance of the metallic surface.
- a method for treating a metallic surface comprises contacting a metallic surface with a medium comprising at least one silicate and providing an alternating current to the medium for a time and under conditions sufficient to improve the corrosion resistance of the metallic surface.
- the silicate can be sodium silicate.
- the medium can comprise water and at least one silicate.
- the metallic surface can comprise at least one member selected from the group consisting of zinc, zinc nickel, tin zinc, and zinc iron.
- the step of providing the alternating current to the medium comprises contacting the metallic surface with an alternating current while the metallic surface is at least partially in contact with the medium.
- FIG. 1 is a schematic of the apparatus and electrical system that can be used in an AC method of the invention.
- FIG. 2 is a graphical representation of the corrosion resistance of articles treated in accordance with the invention.
- the instant invention relates to using AC current to treat a metallic surface (e.g., to provide the opportunity for all beneficial reactions based upon polarity to occur on the work piece) in a silicate containing medium.
- the metallic surface can comprise an electroplated article (e.g., a zinc plated fastener), discrete components having a metallic surface, metallic or metallic coated sheets or rolls, among other surfaces.
- the silicate containing medium can comprise water, at least one silicate, and optionally additives such as silica.
- An example of a suitable silicate comprises sodium silicate.
- the AC process has the advantages of: 1) no dimensionally stable anode is required and thereby minimizes capital costs for setting up the process, and 2) in this configuration work pieces comprise both sides of the electrical circuit; therefore time efficiency is increased in that finished parts can be processed simultaneously.
- the exposed metallic surface can be rinsed and dried.
- the exposed metallic surface is coated with a film or layer in order to impart improved corrosion resistance, color, and lubricity, among other properties.
- suitable coatings can comprise at least one member selected from the group consisting of latex, epoxy, acrylics, and urethanes, among other coatings.
- FIG. 1 shows the physical components and electrical configuration of the inventive process.
- a barrel process is shown, however, a rack process could utilize a similar electrical circuit.
- Zinc plated rivets were treated in accordance with the following Examples.
- FIG. 2 is a graphical representation of the corrosion resistance of these Groups.
Abstract
A method for providing enhanced corrosion protection of metallic components and surfaces when exposing the metallic component to a silicate medium while applying an AC (Alternating Current) current.
Description
- This application claims priority to U.S. Provisional application No. 60/874,165, filed Dec. 11, 2006, and which is incorporated herein by reference.
- Additionally, the subject matter of the instant invention is related to the following patents and patent applications: U.S. Pat. Nos. 6,149,794; 6,258,243; 6,153,080; 6,322,687; 6,572,756B2; 6,592,738B2; 6,599,643; 6,761,934; 6,753,039; 6,866,896B2; Ser. Nos. 10/211,094; 10/636,904; 10/713,480; and 10/831,581. The applications have been published as Publication Nos. 20030209290, 20050031894, 20040137239 and 20040222105, respectively. The disclosure of the foregoing patents and patent applications are hereby incorporated by reference.
- Not Applicable.
- Enhanced corrosion protection for metallic components and surfaces using a silicate based solution where AC (Alternating Current) current is applied.
- The development and use of silicates as process solutions for electroless, electrolytic (cathodic or anodic) environments are known. The resulting layer from electroless processes tends to be relatively soluble unless a reducing agent is added. DC (Direct Current) processes where the work piece is the cathode or the anode are dependent upon the substrate and or the type of chemistry involved. Typically DC processes are used to the extent that a favorable reaction takes place on the surface based upon whether or not the reaction requires that electrons be contributed to the resulting layer or given up by the surface. Pulse processing has been demonstrated to facilitate some processes such as chrome plating where efficiency can be increased by repeatedly breaking down the cathodic film, which buildup on the surface that is being plated. In pulse processes the work piece is still net cathodic or anodic based upon the chemistry or surface being deposited.
- Prior art processes have employed electrolytic cathodic process to deposit a beneficial layer with improved corrosion resistance on zinc, zinc alloy plated substrates and zinc diecast components. First the deposition of Silicon is not inherently cathodic in nature. Therefore, without wishing to be bound by any theory or explanation, it is believed that the resulting layer is the result of the pH environment created by the cathodic polarity of the surface, not the direct reduction on the surface due to the availability of electrons. In addition, in a DC process there is a companion reaction, which occurs at the anode. This companion reaction may facilitate the beneficial result and in typical Zinc plating where the Zinc+ ions required for plating can be electrically oxidized at the anode for electro-reduction to zinc metal at the cathode. There is a need in this art for an electrolytic process for treating a metallic surface with silicates in order to improve the corrosion resistance of the metallic surface.
- Briefly stated, a method for treating a metallic surface is disclosed. The method comprises contacting a metallic surface with a medium comprising at least one silicate and providing an alternating current to the medium for a time and under conditions sufficient to improve the corrosion resistance of the metallic surface. The silicate can be sodium silicate. The medium can comprise water and at least one silicate. The metallic surface can comprise at least one member selected from the group consisting of zinc, zinc nickel, tin zinc, and zinc iron. In accordance with one aspect of the method, the step of providing the alternating current to the medium comprises contacting the metallic surface with an alternating current while the metallic surface is at least partially in contact with the medium.
-
FIG. 1 is a schematic of the apparatus and electrical system that can be used in an AC method of the invention. -
FIG. 2 is a graphical representation of the corrosion resistance of articles treated in accordance with the invention. - Corresponding reference numerals will be used throughout the several figures of the drawings.
- The following detailed description illustrates the invention by way of example and not by way of limitation. This description will clearly enable one skilled in the art to make and use the invention, and describes several embodiments, adaptations, variations, alternatives and uses of the invention, including what I presently believe is the best mode of carrying out the invention. Additionally, it is to be understood that the invention is not limited in its application to the details of construction and the arrangements of components set forth in the following description or illustrated in the drawings. The invention is capable of other embodiments and of being practiced or being carried out in various ways. Also, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting.
- The instant invention relates to using AC current to treat a metallic surface (e.g., to provide the opportunity for all beneficial reactions based upon polarity to occur on the work piece) in a silicate containing medium. The metallic surface can comprise an electroplated article (e.g., a zinc plated fastener), discrete components having a metallic surface, metallic or metallic coated sheets or rolls, among other surfaces. The silicate containing medium can comprise water, at least one silicate, and optionally additives such as silica. An example of a suitable silicate comprises sodium silicate.
- Experiments using AC current instead of DC have demonstrated an improvement in corrosion performance in ASTM-B-117 corrosion testing. Data collected indicates that an increase in hours to 1st white corrosion of 144% (52 to 127) and an 80% increase in the average time to 5% red failure. Samples for this evaluation came from the same Zinc plating batch. The cathodic process using a sodium silicate solution, process times, process temperature, dry conditions, and current densities in accordance with the previously identified Cross-Referenced Patents and Applications were constants. The processes disclosed therein are incorporated herein by reference. The DC cathodic samples were processed using conventional process equipment. The AC samples were produced using an opposed barrel configuration illustrated in
FIG. 1 . - An experiment wherein the initial current density was tripled yielded an increase in average time to 1st white corrosion of 469%. At 480 hours of exposure only 1 sample out of 20 has reached 5% red rust, whereas all 20 samples from the conventional DC process had failed by 240 hours of exposure.
- The AC process has the advantages of: 1) no dimensionally stable anode is required and thereby minimizes capital costs for setting up the process, and 2) in this configuration work pieces comprise both sides of the electrical circuit; therefore time efficiency is increased in that finished parts can be processed simultaneously.
- The electrical dynamics of AC current are different than the use of pulse rectifiers in that typical pulse sources generate waveforms similar to square waves. In this condition voltage transitions are extremely rapid to a set threshold and remain at the predefined level until rapidly changed again. Conventional AC current is constantly undergoing changes in voltage and current relationships, which can potentially change the chemical response at the surface of the work piece.
- If desired, after exposure to the AC environment, the exposed metallic surface can be rinsed and dried. In some cases, the exposed metallic surface is coated with a film or layer in order to impart improved corrosion resistance, color, and lubricity, among other properties. Examples of suitable coatings can comprise at least one member selected from the group consisting of latex, epoxy, acrylics, and urethanes, among other coatings.
- The configuration of
FIG. 1 . shows the physical components and electrical configuration of the inventive process. A barrel process is shown, however, a rack process could utilize a similar electrical circuit. - The following Examples are provided to illustrate certain aspects of the invention and do not limit the scope of the appended claims.
- Zinc plated rivets were treated in accordance with the following Examples.
- Medium/Solution: 9.8% Sodium Silicate in de-ionized Water
- Temperature: 149° F. (65° C.)
- Time 7.5 min
- Barrel size (2) Lusteron 2″×4″
- Rotation; nominal 12 RPM
- (Corrosion Test—Group 1) Voltage to achieve 2.0 nominal amps 14 VAC
- Current trend. 0 min. 2.9-3.0 amps, 3.5 min. 0.9-1.5 amps, 5.0 min. 0.8-1.0 amps, 7.5 min. 0.8-0.9 amps.
- Rivet appearance shiny
- (Corrosion Test—Group 2) 10 amp target could not be reached stopped increasing voltage at 50 VAC
- As voltage was increased a new short term peak could be reached then would diminish.
-
Current trend 0 min. 6-9 amps, 1 min. 3-4 amps, 3 min. 2.5-4.0 amps, 5 min. 1.5-3.0 amps. - Arcing visible inside barrels, Run terminated at 5 minutes after an arcing event. Continuity testing on the barrel danglers indicated infinite resistance.
- Sanded dangler ends to remove buildup continuity restored
- Dangler in neutral barrel black
- Dangler in L1 barrel amber color
- Rivet appearance dull gray.
- (Corrosion Test—Group 3) Voltage to achieve target 0.6 amps 2 VAC
-
Current trend 0 min. 0.6 amps, 1.5 min. 0.4-0.6 amps, 4 min. 0.3-0.6 amps, 7.5 min. 0.3-0.7 amps. - Rivet appearance shiny
- The following Table summarizes the corrosion resistance of the Group of rivets when measured in accordance with ASTM B-117.
FIG. 2 is a graphical representation of the corrosion resistance of these Groups. -
Part Time Group Group Description Type Part. No. Area N n Min Avg n Min Avg n Min Avg (hours) Group 01 Zinc(AC)EMC Rivets 99020033 Main 20 20 72 127 19 192 289 19 216 322 648 AC Process 2 amps 7.5 min. D/R/D Group 02 Zinc(AC)EMC Rivets 99020033 Main 20 17 96 315 3 384 520 3 432 560 648 AC Process 6 amps 7.5 min. D/R/D Group 03 Zinc(AC)EMC Rivets 99020033 Main 20 20 24 104 20 144 253 20 144 276 504 AC Process 0.6 amps 7.5 min. D/R/D Group 04 Zinc Typical Rivets 99020033 Main 20 20 24 52 20 120 157 20 144 172 240 DC Process Line #3 EMC 22 amps 7.5 D/R/D - In view of the above, it will be seen that the several objects and advantages of the present invention have been achieved and other advantageous results have been obtained.
- As various changes could be made in the above constructions without departing from the scope of the invention, it is intended that all matter contained in the above description or shown in the accompanying drawings shall be interpreted as illustrative and not in a limiting sense.
Claims (5)
1) A method for treating a metallic surface comprising:
contacting a metallic surface with a medium comprising at least one silicate, and;
providing an alternating current to the medium for a time and under conditions sufficient to improve the corrosion resistance of the metallic surface.
2) The method of claim 1 wherein the silicate comprises sodium silicate.
3) The method of claim 1 wherein the medium comprises water and at least one silicate.
4) The method of claim 1 wherein the metallic surface comprises at least one member selected from the group consisting of zinc, zinc nickel, tin zinc, and zinc iron.
5) The method of claim 1 wherein the providing comprises contacting the metallic surface with an alternating current while the metallic surface is at least partially in contact with the medium.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US11/953,441 US20080135135A1 (en) | 2006-12-11 | 2007-12-10 | Method For Treating Metallic Surfaces With an Alternating Electrical Current |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US87416506P | 2006-12-11 | 2006-12-11 | |
US11/953,441 US20080135135A1 (en) | 2006-12-11 | 2007-12-10 | Method For Treating Metallic Surfaces With an Alternating Electrical Current |
Publications (1)
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US20080135135A1 true US20080135135A1 (en) | 2008-06-12 |
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US11/953,441 Abandoned US20080135135A1 (en) | 2006-12-11 | 2007-12-10 | Method For Treating Metallic Surfaces With an Alternating Electrical Current |
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WO (1) | WO2008073887A2 (en) |
Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3335074A (en) * | 1964-05-14 | 1967-08-08 | Cons Mining & Smelting Co | Anodic treatment of zinc and zinc-base alloys |
US6149794A (en) * | 1997-01-31 | 2000-11-21 | Elisha Technologies Co Llc | Method for cathodically treating an electrically conductive zinc surface |
US6153080A (en) * | 1997-01-31 | 2000-11-28 | Elisha Technologies Co Llc | Electrolytic process for forming a mineral |
US6322687B1 (en) * | 1997-01-31 | 2001-11-27 | Elisha Technologies Co Llc | Electrolytic process for forming a mineral |
US6592738B2 (en) * | 1997-01-31 | 2003-07-15 | Elisha Holding Llc | Electrolytic process for treating a conductive surface and products formed thereby |
US6599643B2 (en) * | 1997-01-31 | 2003-07-29 | Elisha Holding Llc | Energy enhanced process for treating a conductive surface and products formed thereby |
US20030209290A1 (en) * | 2001-08-03 | 2003-11-13 | Heimann Robert L. | Process for treating a conductive surface and products formed thereby |
US6753039B2 (en) * | 2001-08-03 | 2004-06-22 | Elisha Holding Llc | Electrolytic and electroless process for treating metallic surfaces and products formed thereby |
US6761934B2 (en) * | 2001-08-03 | 2004-07-13 | Elisha Holding Llc | Electroless process for treating metallic surfaces and products formed thereby |
US20040137239A1 (en) * | 2002-11-14 | 2004-07-15 | Klaus-Peter Klos | Processes for electrocoating and articles made therefrom |
US20040222105A1 (en) * | 2003-04-25 | 2004-11-11 | Heimann Robert L. | Method for preparing and using silicate systems to treat electrically conductive surfaces and products obtained therefrom |
US20050031894A1 (en) * | 2003-08-06 | 2005-02-10 | Klaus-Peter Klos | Multilayer coated corrosion resistant article and method of production thereof |
US6866896B2 (en) * | 2002-02-05 | 2005-03-15 | Elisha Holding Llc | Method for treating metallic surfaces and products formed thereby |
US6919012B1 (en) * | 2003-03-25 | 2005-07-19 | Olimex Group, Inc. | Method of making a composite article comprising a ceramic coating |
-
2007
- 2007-12-10 WO PCT/US2007/086970 patent/WO2008073887A2/en active Application Filing
- 2007-12-10 US US11/953,441 patent/US20080135135A1/en not_active Abandoned
Patent Citations (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3335074A (en) * | 1964-05-14 | 1967-08-08 | Cons Mining & Smelting Co | Anodic treatment of zinc and zinc-base alloys |
US6149794A (en) * | 1997-01-31 | 2000-11-21 | Elisha Technologies Co Llc | Method for cathodically treating an electrically conductive zinc surface |
US6153080A (en) * | 1997-01-31 | 2000-11-28 | Elisha Technologies Co Llc | Electrolytic process for forming a mineral |
US6258243B1 (en) * | 1997-01-31 | 2001-07-10 | Elisha Technologies Co Llc | Cathodic process for treating an electrically conductive surface |
US6322687B1 (en) * | 1997-01-31 | 2001-11-27 | Elisha Technologies Co Llc | Electrolytic process for forming a mineral |
US6572756B2 (en) * | 1997-01-31 | 2003-06-03 | Elisha Holding Llc | Aqueous electrolytic medium |
US6592738B2 (en) * | 1997-01-31 | 2003-07-15 | Elisha Holding Llc | Electrolytic process for treating a conductive surface and products formed thereby |
US6599643B2 (en) * | 1997-01-31 | 2003-07-29 | Elisha Holding Llc | Energy enhanced process for treating a conductive surface and products formed thereby |
US20030209290A1 (en) * | 2001-08-03 | 2003-11-13 | Heimann Robert L. | Process for treating a conductive surface and products formed thereby |
US6753039B2 (en) * | 2001-08-03 | 2004-06-22 | Elisha Holding Llc | Electrolytic and electroless process for treating metallic surfaces and products formed thereby |
US6761934B2 (en) * | 2001-08-03 | 2004-07-13 | Elisha Holding Llc | Electroless process for treating metallic surfaces and products formed thereby |
US6866896B2 (en) * | 2002-02-05 | 2005-03-15 | Elisha Holding Llc | Method for treating metallic surfaces and products formed thereby |
US20040137239A1 (en) * | 2002-11-14 | 2004-07-15 | Klaus-Peter Klos | Processes for electrocoating and articles made therefrom |
US6919012B1 (en) * | 2003-03-25 | 2005-07-19 | Olimex Group, Inc. | Method of making a composite article comprising a ceramic coating |
US20040222105A1 (en) * | 2003-04-25 | 2004-11-11 | Heimann Robert L. | Method for preparing and using silicate systems to treat electrically conductive surfaces and products obtained therefrom |
US20050031894A1 (en) * | 2003-08-06 | 2005-02-10 | Klaus-Peter Klos | Multilayer coated corrosion resistant article and method of production thereof |
Also Published As
Publication number | Publication date |
---|---|
WO2008073887A2 (en) | 2008-06-19 |
WO2008073887A3 (en) | 2008-07-31 |
WO2008073887A9 (en) | 2008-09-12 |
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Legal Events
Date | Code | Title | Description |
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AS | Assignment |
Owner name: ELISHA HOLDING LLC, MISSOURI Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SOUCIE, WAYNE;WINN, DENNIS;DALTON, WILLIAM;REEL/FRAME:020257/0083 Effective date: 20071210 |
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STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |