EP0056331B1 - Process and apparatus for treating electrically conductive matrices and products produced by the process - Google Patents

Process and apparatus for treating electrically conductive matrices and products produced by the process Download PDF

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Publication number
EP0056331B1
EP0056331B1 EP82300138A EP82300138A EP0056331B1 EP 0056331 B1 EP0056331 B1 EP 0056331B1 EP 82300138 A EP82300138 A EP 82300138A EP 82300138 A EP82300138 A EP 82300138A EP 0056331 B1 EP0056331 B1 EP 0056331B1
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Prior art keywords
matrix
conductive element
sem
solution
fusion
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EP82300138A
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German (de)
French (fr)
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EP0056331A1 (en
Inventor
Joseph Ady
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Metafuse Ltd
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Metafuse Ltd
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C20/00Chemical coating by decomposition of either solid compounds or suspensions of the coating forming compounds, without leaving reaction products of surface material in the coating
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/18Electroplating using modulated, pulsed or reversing current
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C25D17/10Electrodes, e.g. composition, counter electrode
    • C25D17/14Electrodes, e.g. composition, counter electrode for pad-plating
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/60Electroplating characterised by the structure or texture of the layers
    • C25D5/605Surface topography of the layers, e.g. rough, dendritic or nodular layers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/60Electroplating characterised by the structure or texture of the layers
    • C25D5/623Porosity of the layers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/627Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance

Definitions

  • the present invention relates to fusion processes, apparatus for carrying out such processes and the products of such processes.
  • fusion is employed as meaning a process whereby diverse elements are chemically or physically bonded.
  • the workpiece or matrix may be of a certain form which does not lend itself to the subjection of a particular characteristic-enhancing process;-the process may be destructive of the already desirable characteristics of the work-piece; or the treated work-piece while having certain enhanced characteristics may exhibit other reduced characteristics.
  • the process employed depends upon the work-piece or matrix to be treated and the characteristics desired.
  • coating techniques heat treatment, anodizing, arc spraying, vaccum evaporation, chemical deposition, sputtering, and ion plating are all common processes.
  • Non-ferrous metals may be hardened by aging, heat treatment or anodizing.
  • Spray coating techniques have not improved corrosion resistance or the physical properties of ferrous materials.
  • the other techniques arc-spraying, vaccum evaporation and sputtering have their shortcomings in that the coating deposited is usually thin, the interfacial bond strength is poor, or can only be used to treat small surface areas.
  • U.S. Application No. 3743590 discloses an electroplating device having a continuously rotating anode with a continuous supply of plating solution provided through the anode to provide optimum plating.
  • first conductive element shall refer to the matrix with which fusion is to be accomplished; and the term “chemical element” shall refer to such an element or an alloy thereof; the term “second conductive element or an alloy thereof” shall refer to the element which is to be fused with the matrix.
  • fusion means a penetration by the atoms or molecules of a second element within the solid matrix of a first element or alloy thereof.
  • Solutions for use in the process and in association with the apparatus may comprise a solution of a conductive chemical of the chemical to be fused in a dissociable form which may be present in the range of 0.10% to 10% by weight and having a pH in the range of 0.4 to 14.
  • the resistivity of the solution is in the range of 5 to 500 ohms cm, preferably 10 to 80 ohms cm.
  • One side of the oscillator output is connected to an electrode 13 through a holder 12.
  • Holder 12 is provided with a rotating chuck and has a trigger switch which controls the speed of rotation of the electrode 13.
  • the speed of rotation is variable from 5,000 to 10,000 rpm.
  • the electrode 13 is composed of the material to be fused with the matrix.
  • the matrix or substrate which is to be subjected to the process and which is to be treated is indicated at 14.
  • the matrix is also connected to the other side of the oscillator output by a clamp 15 and line 16.
  • the electrode is positively charged and the matrix is negatively charged when the signal is applied.
  • the process employed may be characterized as a liquid to solid process.
  • the material to be fused is in the form of a solution and is held in a reservoir 17.
  • Reservoir 17 is connected by a tube 18 to an electrode 19.
  • Electrode 19 is a plate provided with an insulated handle 20 through which one side of oscillator 11 output is connected. This output is led into a main channel 21 in electrode 19.
  • Channel 21 has a series of side channels 22 which open on to the undersurface of electrode 20.
  • the flow from reservoir 17 is by gravity or by a pump and may be controlled by a valve such as 23 on the handle 20.
  • the surface of electrode 19 is preferably covered by a permable membrane such as cotton or nylon.
  • the operator passes the rotating electrode 13 in contact with the upper surface of the matrix over the matrix surface at a predetermined speed to apply the electrode material to the matrix and fuse it therewith.
  • both the matrix and the material to be applied have specific resistance characteristics. Thus with each change in either one or both of these- materials there is a change in the resistivity of the circuit.
  • a signal having an amplitude of 3 amps is believed to be the preferred amplitude. If the amplitude is greater decarbonizing or burning of the matrix takes place and below this amplitude hydroxides are formed in the interface.
  • FIG. 4 is a schematic diagram of an oscillator circuit used in apparatus in accordance with the present invention.
  • a power supply 30 is connected across the input, and across the input a capacitor 31 is connected.
  • One side of the capacitor 31 is connected through the LC circuit 32 which comprises a variable inductance coil 33 and capacitor 34 connected in parallel.
  • LC circuit 32 is connected to one side of a crystal oscillator circuit comprising crystal 35, inductance 36, NPN transistor 37 and the RC circuit comprised of variable resistance 38 and capacitance 39.
  • This oscillator circuit is connected to output 50 through, on one side capacitor 40, and on the other side diode 41, to produce a halfwave signal across output 50.
  • the travel speed may be determined by the following form:
  • resistances R 1 and R 2 may be measured by any known means.
  • the speed of rotation is also believed to affect the quality of the fusion with a rotation speed of 5,000 rpm the finish is an uneven 200 to 300 finish; with a speed of rotation of 10,000 rpm the finish is a substantially 15 p finish.
  • the apparatus of Figure 2 is operated in the same manner as the apparatus of Figure 1 and the process is essentially the same except for the use of a liquid with a solid electrode.
  • the solid to solid process is illustrated by Examples I, II, IIA, III, and IV.
  • Figures 9, 10 and 11 give spectra from the parent metal.
  • Figures 12 through 16 show the presence of a small titanium peak which does not change markedly in height as the zone was crossed.
  • the approximate width of the zone in which titanium was detected is about 50 m although this dimension varied along the specimen length.
  • 1018 Steel was connected to the apparatus of Figure 1 as the matrix 14 and the electrode 13 was molybdenum, Type Mo 1.
  • the steel was 12.7 mm widex6.35 mm thickx38.1 mm long, the molybdenum 25.4 mm longx4 mm diameter.
  • the frequency applied was 43.31 KHz and the speed of electrode rotation approximately 12,000 rpm.
  • the surface of the steel was ground to a surface finish of 600 grit.
  • the electrode tip was moved manually along the top surface of the steel sample in straight lines adjacent to each other. The process was repeated at 90° to cover the whole surface. Under the optical microscope at x40 magnification small beads of melted and resolidified material were revealed.
  • the average KHN of the untreated steel was 188.
  • the hardness of the same steel after heating to 900°C and water quenching was 285 (KHN) at 200 gm.
  • Example II The same matrix and electrode and procedure as in Example II were followed at a frequency of 30.60 3 KHz and the same speed of rotation.
  • the frequency applied was 26.20 KHz and the speed of electrode rotation was approximately 12,000 rpm.
  • tungsten is shown to be fused with the steel matrix.
  • the results of an electron microscope analysis across the sample indicate the presence of tungsten to a depth of at least 80 pm and are shown in Figure 21 and the following table:
  • the hardness of the untreated sample is approximately 188 KHN and after heating to 900°C and quenching was 285 KHN.
  • the matrix 14 metal was connected into the circuit as previously described.
  • the frequency was determined in accordance with the formula previously set forth and the solution in reservoir 17 applied by movement of the electrode over one surface of the first metal for varying periods of time as determined by Form II.
  • the electrode was covered with cotton gauze or nylon. It will be apparent that other materials may be employed. This arrangement also served to limit contamination of the solution when graphite electrodes were employed. They had a tendency to release graphite particles in the course of movement.
  • the sample was etched using Nital for steel, the ferrous substrate, and Ammonium Hydrogen Peroxide on the copper, the non-ferrous substrate.
  • a semiquantitative electron probe microanalysis of fused interfaces were performed using an Energy Dispersive X-Ray Spectroscopy (EDX) and a Scanning Electron Microscope (SEM).
  • EDX Energy Dispersive X-Ray Spectroscopy
  • SEM Scanning Electron Microscope
  • the surface of the embedding plastic was rendered conductive by evaporating on it approximately 20 pm layer of carbon in a vacuum evaporator. This procedure was used to prevent buildup of electrical charges on an otherwise nonconductive material and a consequent instability of the SEM image. Carbon, which does not produce a radiation detectable by the EDX, was used in preference of a more conventional metallic coating to avoid interference of such a coating with the elemental analysis.
  • the diameter of analysed volume was calculated for typical elements analysed and was found to be as follows:
  • the second conductive chemical element that is the element to be diffused into the matrix
  • small quantities of metallic ions of a third metal are also provided.
  • the presence of these metal ions is believed to be required as complex forming agents to facilitate fusion.
  • Small quantities of organic catalysts such as gum acacia, hydroquinone, animal glue, pepsin, dextrin, licorice, or their equivalents may also be present.
  • wetting agents such as sodium lauryl sulphate or its equivalent are usually provided.
  • pH varying agents such as ammonium hydroxide or sulphuric acid are usually added to reach an operating pH.
  • second chemical conductive element complexing agents which preclude precipitation of the second element.
  • These agents were by way of example citric acid, or sodium pyrophosphate, or ethyldiaminetetracetic acid or their equivalents.
  • a suitable buffer is also provided in certain solutions, where required.
  • the water is always demineralized.
  • Atlas A151 1020 steel was connected in the apparatus of Figure 2 as the matrix 14 and a 10% solution of ammonium molybdate in water was placed in reservoir 17.
  • Example IV The sample of Example IV was subject to a thermal corrosion test. 25% sulphuric acid was applied to the surface for 20 minutes at 325°C without any surface penetration.
  • the Mo +6 concentration may be varied from 1.5% to 2.5% by weight; the pH from 7.2 to 8.2 and the resistivity from 17-25 ohms cm.
  • the photomicrograph Figure 24 shows the deposition of a substantially uniform layer of molybdenum 1 micron thick of uniform density.
  • an SEM/EPMA scan across the interface between the substrate and the applied metal shows molybdenum was present to a depth of at least 10 microns and a molybdenum gradient as set out below in Table.
  • the solution had the following characteristics:
  • the W +6 concentration may vary from 1.6% to 2.5%; the pH may vary from 7.5 to 8.5; and the resistivity may vary from 18 ohms cm to 24 ohms cm.
  • the sample showed a uniform deposit of tungsten approximately 1 micron thick.
  • An SEM/EPMA scan showed fusion of tungsten on copper to a depth of at least 5.0 microns, as can be seen in the Table below and Figure 28.
  • the concentration of tungsten may be varied from 1.6% to 2.5% by wt.; the pH from 7.5 to 8.5; and the conductivity from 18.8 ohms cm to 22.8 ohms cm.
  • the solution had the following characteristics: The Indium concentration may vary from 0.2% to 2.2%; the pH from 1.60 to 1.68; and the resistivity from 48.8 ohms cm to 54.8 ohms cm.
  • Example IX The solution of Example IX was employed and applied to a steel matrix:
  • Figure 35 shows a solid deposit of nickel of uniform density approximately 1.5 pm thick.
  • an SEM/EPMA scan across the interface between the matrix and the nickel layer shows nickel to be fused to a depth of at least 4 ⁇ m.
  • aqueous solution of the following formulation was prepared: The solution had the following characteristics: The nickel concentration may vary from 2% to 10%; pH from 3.10 to 3.50; and resistivity from 17 ohms cm to 26 ohms cm.
  • Example XI The same solution as was formulated for Example XI was prepared and applied to a steel matrix:
  • the nickel layer is continuous and substantially uniform in thickness being about 1.5 ⁇ m thick.
  • nickel is shown to be fused to a depth of at least 3 ⁇ m.
  • aqueous solution of the following formulation was prepared: This solution had the following characteristics: The pH may be varied from 3.70 to 11; the concentration of Au +3 ions may vary from 0.1% to 0.5% by weight; and the resistivity from 40 ohms cm to 72 ohms cm. Observation with the optical and scanning electron microscope revealed a surface deposition of gold approximately 1.5 ⁇ m thick. The deposit was continuous and uniformly dense as shown in Figure 39.
  • An SEM/EPMA scan across the interface indicated fusion of gold to a depth of at least 3 ⁇ m as shown on the Table below and Figure 40.
  • Example XIII An aqueous solution of the same formulation as that of Example XIII was prepared: Observation with the optical and scanning electron microscope revealed a surface deposition of gold approximately 1.0 ⁇ m thick. The deposit was uniformly thick and dense as shown in Figure 41.
  • An SEM/EPMA scan across the interface indicated fusion of gold to a depth of at least 4.0 ⁇ m as shown on the table below and Figure 42.
  • the pH may be varied from 0.6 to 1.0: the concentration of Cr +6 ions may vary from 3% to 20% by weight; and the resistivity from 11 ohms cm to 14 ohms cm. Observation with the optical and scanning electron microscope revealed a surface deposition of chromium approximately 1 pm thick. The surface of the layer was irregular but the deposit appeared free of faults and was continuous as shown in Figure 43.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 3.0 ⁇ m as shown on the table below and Figure 44.
  • Example XV An aqueous solution of the same formulation as employed in Example XV was prepared: Observation with the optical and scanning electrode microscope revealed a surface deposition of chromium approximately 3.0 ⁇ m thick. This is as shown in Figure 45.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 5.0 ⁇ m as shown on the Table below and Figure 46.
  • aqueous solution of the following formulation was prepared: This solution had the following characteristics: The pH may be varied from 2.5 to 3.5; the concentration of Cr +3 ions may vary from 1.8% to 5% by weight; and the resistivity from 16 ohms cm to 20 ohms cm. Observation with the optical and scanning electron microscope revealed a surface deposition of chromium approximately 0.5 ⁇ m thick. The deposit was solid and continuous as shown in Figures 47 and 47A.
  • An SEM/EPMA scan across the interface indicated fusion of chromium ta a depth of at least 3.0 ⁇ m as shown on the Table below and Figure 48.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 3.0 ⁇ m as shown on the Table below and Figure 50.
  • the pH may be varied from 10 to 10.2; the concentration of Cd +2 ions may vary from 0.2% to 0.5% by weight; and the resistivity from 28 ohms cm to 35 ohms cm.
  • the solution employed was initially as set out above, applied in accordance with the conditions identified as (1).
  • a second solution, that set forth in Example XX, was then applied under the conditions identified as (2).
  • Observation with the optical and scanning electron microscope revealed a surface deposition of cadmium approximately 4 p m thick. This deposit was not homogeneous as shown in Figure 51 but an SEM/EPMA scan across the interface indicated fusion of cadmium to a depth of at least 9 ⁇ m as shown on the Table below and Figure 52.
  • the pH may be varied from 3.2 to 3.5; the concentration of Cd +2 ions may vary from 1 % to 4% by weight; and the resistivity from 45 ohms cm to 55 ohms cm.
  • the pH may be varied from 11.2 to 12.7; the concentration of Sn +2 ions may vary from 2% to 5% by weight; and the resistivity from 6.2 ohms cm to 10.3 ohms cm.
  • An SEM/EPMA scan across the interface indicated fusion of tin to a depth of at least 4 ⁇ m as shown on the table below and Figure 56.
  • the pH may be varied from 9 to 9.7; the concentration of Sn +2 ions may vary from 0.4% to 1% by weight; and the resistivity from 30 ohms cm to 36 ohms cm.
  • An SEM/EPMA scan across the interface indicated fusion of tin to a depth of at least 5 ⁇ m as shown on the Table below and Figure 58.
  • Example XXII An aqueous solution of the same as prepared for Example XXII was employed: Observation with the optical and scanning electron microscope revealed a surface deposition of tin exceeding 2 ⁇ m thick. This layer was porous but continuous as shown in Figure 59.
  • the pH may be varied from 4.5 to 6.5 the concentration of Co +2 ions may vary from 2% to 6% by weight; and the resistivity from 25 ohms cm to 30 ohms cm.
  • Observation with the optical and scanning electron microscope revealed a surface deposition of cobalt approximately 6.5 pm thick. This layer was uniform and continuous as shown in Figure 61.
  • the pH may be varied from 11.2 to 11.7; the concentration of Ag +1 ions may vary from 1% to 3% by weight; and the resistivity from 8 ohms cm to 13 ohms cm.
  • An SEM/EPMA scan across the interface indicated fusion of silver to a depth of at least 3 ⁇ m as shown on the Table below and Figure 64.
  • the pH may be varied from 1.5 to 2; the concentration of Ag +1 ions may vary from 0.5% to 2.5% by weight; and the resistivity from 6 ohms cm to 12 ohms cm.
  • An SEM/EPMA scan across the interface indicated fusion of silver to a depth of at least 2.00 J.lm as shown on the Table below and Figure 66.
  • tin, gold and silver with their inherent excellent conductivity characteristics may be employed in electrical applications and circuits may be fused on other substrates.
  • the anti-corrosion characteristics of tin, gold, silver, nickel, chromium, cadmium, molybdenum and tungsten are also useful. And the application of those metals to ferrous or non-ferrous substrates will enhance their anti-corrosion behavior.
  • Chromium, nickel, silver, gold or tin have the capability of imparting an elegant appearance to the matrix. Chromium, molybdenum, tungsten, titanium and cobalt impart a surface hardness to the matrix.
  • Indium imparts strength to the matrix, and also serves as anti-galling agent.
  • a molybdenum treated ferrous or non-ferrous matrix has improved friction-wear and high temperature resistance characteristics. It is also useful as a dielectric coating.
  • a cadmium fused matrix as well as having enhanced corrosion resistance characteristics can also serve as an anti-fouling agent for ship hull treatment.
  • Silver fused matrices are all useful as a reflecting medium.

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Description

  • The present invention relates to fusion processes, apparatus for carrying out such processes and the products of such processes.
  • It will be understood that for the purposes of this application that the term "fusion" is employed as meaning a process whereby diverse elements are chemically or physically bonded.
  • It has been a common practice to treat substrates or matrices in different manners to enhance the characteristics of the matrix for a particular application. Sometimes these treatments have involved the matrix as a body and in other techniques only the surface characteristics are enhanced.
  • However, these techniques have had limitations. The workpiece or matrix may be of a certain form which does not lend itself to the subjection of a particular characteristic-enhancing process;-the process may be destructive of the already desirable characteristics of the work-piece; or the treated work-piece while having certain enhanced characteristics may exhibit other reduced characteristics.
  • Generally, the process employed depends upon the work-piece or matrix to be treated and the characteristics desired.
  • More specifically, coating techniques, heat treatment, anodizing, arc spraying, vaccum evaporation, chemical deposition, sputtering, and ion plating are all common processes.
  • Non-ferrous metals may be hardened by aging, heat treatment or anodizing.
  • These techniques however, do not provide adequate protection against dry rubbing wear.
  • Spray coating techniques have not improved corrosion resistance or the physical properties of ferrous materials.
  • The wear resistance of non-ferrous substrates have been improved by electrochemical or electromechanical plating with hard chromium but these are expensive and time consuming.
  • The other techniques arc-spraying, vaccum evaporation and sputtering have their shortcomings in that the coating deposited is usually thin, the interfacial bond strength is poor, or can only be used to treat small surface areas.
  • They have disadvantages in use in that they employ gaseous techniques or high voltages which are difficult in practice and limit their versatility.
  • In plating, Volume 56, No. 8 August 1969 pages 909-913 there is disclosed an electroplating process involving the electrodeposition of copper and silver from a copper or silver bath by use of pulsed direct current. The process was directed to the problem of making very thin electroformed foils but the results were unsatisfactory.
  • U.S. Application No. 3743590 discloses an electroplating device having a continuously rotating anode with a continuous supply of plating solution provided through the anode to provide optimum plating.
  • According to the present invention there is provided a process for the fusion, at an ambient temperature, of at least one second conductive element comprising ferrous or non-ferrous metals or alloys thereof into a matrix of a first conductive element comprising a ferrous or non-ferrous metal or alloys thereof, said process comprising the steps of
    • (a) bringing said second conductive element into contact with a limited area of an adjacent surface of said first conductive element,
    • (b) applying a half-wave interrupted pulsing signal in the range of 2.5 microseconds to 28.6 nanoseconds with a frequency of 400 Hz to 35 MHz and an amplitude of about 3 amps over an area of about 0.3 square mm, and
    • (c) fusing said second conductive element in said first conductive element to a depth of more than 0.5 pm and depositing a surface layer of said second chemical element of more than 0.5 pm thickness.
  • For convenience of reference, in this description, the term "first conductive element" shall refer to the matrix with which fusion is to be accomplished; and the term "chemical element" shall refer to such an element or an alloy thereof; the term "second conductive element or an alloy thereof" shall refer to the element which is to be fused with the matrix.
  • It will also be understood that the term "fusion" as used in this specification means a penetration by the atoms or molecules of a second element within the solid matrix of a first element or alloy thereof.
  • Thus, there is provided in accordance with the present invention a process for altering the surface properties of a metal or alloy thereof at ambient temperatures by physically applying a second conductive chemical element to the surface whose characteristics are to be varied and applying an intermittent electrical signal of a predetermined frequency to both elements when they are in physical contact.
  • Solutions for use in the process and in association with the apparatus may comprise a solution of a conductive chemical of the chemical to be fused in a dissociable form which may be present in the range of 0.10% to 10% by weight and having a pH in the range of 0.4 to 14. Advantageously, the resistivity of the solution is in the range of 5 to 500 ohms cm, preferably 10 to 80 ohms cm.
  • By the application of the process to ferrous or non-ferrous matrices new products are produced, in which a second chemical conductive element is fused in a first chemical conductive element to a depth of more than 0.5 pm and a surface layer of the second chemical conductive element has been deposited to heights exceeding 0.5 Jlm.
  • These and other objects and features of the present invention will become more apparent from the following description and drawings in which certain specific embodiments of the process apparatus and products of the process are illustrative of the invention and in which:
    • Figure 1 is a general perspective view of one embodiment of the apparatus in accordance with the invention being used in accordance with a process of the present invention;
    • Figure 2 is a general perspective view of a second embodiment of an apparatus in accordance with the invention being used in accordance with a process of the invention;
    • Figure 3 is a schematic electrical circuit employed in the present invention;
    • Figure 4 is a circuit diagram of an oscillator as employed in apparatus in accordance with one embodiment of the present invention;
    • Figure 5 is a photomicrograph with a magnification of x500 of a section of steel treated in accordance with the present invention with titanium carbide;
    • Figure 6 is a photomicrograph with a magnification x110 showing the penetration of titanium in the treated specimen of Figure 5;
    • Figure 7 is an electron probe microanalyser (EPMA) Ti K x-ray scan x450 across the surface layer of the specimen whose section is shown in Figures 5 and 6;
    • Figure 8 is a photomicrograph with a magnification x 1100 of the specimen illustrated in Figure 5 after heavy nickel plating and polishing and serves to show the deposit thickness;
    • Figures 9 through 16 are EPMA line scans from each of the locations 1 through 8, respectively, as shown in Figure 5;
    • Figure 17 is an EPMA scan of the Ti rich zone marked in Figure 8;
    • Figure 18 is a composite photomicrograph taken with a scanning electron microscope (SEM) with right and left hand halves of a steel matrix with which molybdenum has been fused using the process of the present invention with a solid molybdenum electrode; the left hand half has a magnification x655 and the right hand half is a x1965 enlargement of the marked area of the left hand half;
    • Figure 18A is a composite photomicrograph with right and left hand halves of a further steel matrix with which molybdenum has been fused using the process of the present invention with a solid molybdenum electrode; the left hand half has a magnification x1310 and the right hand half is x3930 enlargement of the marked area of the left hand half;
    • Figure 19 is a graph of an SEM/EPMA across the sample shown in Figure 18 and shows the fusion of the molybdenum with steel;
    • Figure 19A is a graph of an electron microscope scan across the sample shown in Figure 19 and shows the fusion of molybdenum with steel;
    • Figure 20 is a SEM photomicrograph with a magnification x 1310 of a steel matrix with which tungsten has been fused using the process of the present invention with a solid tungsten electrode;
    • Figure 21 is a graph of an SEM/EPMA scan across the sample shown in Figure 20 and shows the fusion of tungsten with the steel;
    • Figure 22 is a composite SEM photomicrograph with right-hand and left-hand halves, of a copper matrix with which molybdenum has been fused using the process of the present invention with a molybdenum solution. The left-hand half has a magnification x1250 and the right-hand half is a x8 enlargement of the marked area of the left-hand half.
    • Figure 23 is a graph of an SEM/EPMA scan across the sample shown in Figure 22 and shows the fusion of molybdenum with copper;
    • Figure 24 is a composite SEM photomicrograph, with right and left hand halves, of a steel matrix with which molybdenum has been fused using the process of the present invention with a molybdenum solution. The left hand half has a magnification x1250 and the right hand half is a x8 enlargement of the marked area of the left hand half;
    • Figure 25 is a graph of an SEM/EPMA scan across the sample shown in Figure 24 and shows the fusion of molybdenum with steel;
    • Figure 26 is a composite photomicrograph, with right and left hand halves, of a copper matrix with which tungsten has been fused using the process of the present invention with a tungsten solution. The left hand half has a magnification x1250 and the right hand half is a x8 enlargement of the marked area of the left hand half;
    • Figure 27 is a further SEM photomicrograph of the sample of Figure 26 with a magnification × 10,000of part of the marked area of Figure 26;
    • Figure 28 is a graph of an SEM/EPMA scan across the sample shown in Figures 26 and 27;
    • Figure 29 is a composite photomicrograph, with right and left hand halves, of a steel matrix with which tungsten has been fused using the process of the present invention with a tungsten solution. The left hand half has a magnification x1310 and the right hand half is a x8 enlargement of the marked area of the left hand half;
    • Figure 30 is a graph of an SEM/EPMA scan across the sample shown in Figure 29 and shows the fusion of tungsten with steel;
    • Figure 31 is a composite photomicrograph with right and left hand halves, of a copper matrix with which indium has been fused using the process of the present invention with an indium solution. The left hand half has a magnification x1250 and.the right hand half is a x8 enlargement of the marked section of the left hand half;
    • Figure 32 is a graph of an electron microprobe scan across the sample shown in Figure 31;
    • Figure 33 is a composite SEM photomicrograph, with right and left hand halves of a steel matrix with which indium has been fused using the process of the present invention with an indium solution. The left hand half has a magnification x625 and the right hand half is a x8 enlargement of the marked section of the left hand half;
    • Figure 34 is a graph of an SEM/EPMA scan across the sample shown in Figure 33;
    • Figure 35 is a composite SEM photomicrograph, with right and left hand halves, of a copper matrix with which nickel has been fused using the process of the present invention with a nickel solution. The left hand half has a magnification x1250 and the right hand half is a x8 enlargement of the marked section of the left hand half;
    • Figure 36 is a graph of an SEM/EPMA scan across the sample shown in Figure 35;
    • Figure 37 is a composite SEM photomicrograph with right and left hand halves, of a steel matrix with which nickel has been fused using the process of the present invention with a nickel solution. The left hand half has a magnification x1310 and the right hand half is a x8 enlargement of the marked section of the left hand half;
    • Figure 38 is a graph of an SEM/EPMA scan across the sample shown in Figure 37;
    • Figure 39 is a composite photomicrograph of a copper matrix with which gold has been fused. The left hand half has a magnification x1310 and the right hand half is a x8 enlargement of the marked section of the right hand half.
    • Figure 40 is a graph of an SEM/EPMA scan across the sample shown in Figure 39 showing gold fused in the copper matrix;
    • Figure 41 is a composite photomicrograph with right and left hand halves, of a steel matrix with which gold has been fused using the process of the present invention with a gold solution. The left hand half has a magnification x 1310, the right hand half is x8 magnification enlargement of the marked area of the left hand half;
    • Figure 42 is a graph of an SEM/EPMA scan across the sample shown in Figure 40 showing gold fused in the steel matrix;
    • Figure 43 is an SEM photomicrograph with a magnification x10,000 of a copper matrix with which chromium has been fused using the process of the present invention with a first chromium solution;
    • Figure 44 is a graph of an SEM/EPMA scan across the sample shown in Figure 43 and shows the fusion of chromium with copper;
    • Figure 45 is an SEM photomicrograph with a magnification x10,000 of a steel matrix with which chromium has been fused using the process of the present invention with the first chromium solution referred to above;
    • Figure 46 is a graph of an SEM/EPMA scan across the sample shown in Figure 45 and shows the fusion of chromium with steel;
    • Figure 47 is a composite SEM photomicrograph, with right and left hand halves, of a copper matrix with which chromium has been fused using the process of the present invention with a second chromium solution. The left hand half has a magnification x625 and the right hand half is a x8 enlargement of the marked area of the left hand half;
    • Figure 47A is a further enlarged SEM photomicrograph of the enlarged area of Figure 47 at a magnification of x10,000;
    • Figure 48 is a graph of an SEM/EPMA scan across the sample shown in Figure 47 and shows the fusion of chromium with copper;
    • Figure 49 is a composite SEM photomicrograph, with right and left hand halves, of a steel matrix with which chromium has been fused using the process of the present invention with a second chromium solution. The left hand half has a magnification x 1250 and the right hand half is a x8 enlargement of the marked area of the left hand half;
    • Figure 49A is a further enlarged SEM photomicrograph of the enlarged area of Figure 49 at a magnification of x10,000;
    • Figure 50 is a graph of an SEM/EPMA scan across the sample shown in Figure 48 and shows the fusion of chromium with steel;
    • Figure 51 is a composite photomicrograph with right and left hand halves, of a copper matrix with which cadmium has been fused using the process of the present invention with a first cadmium solution; the left hand half has a magnification x1310 and the right hand half is a x5 enlargement of the marked area;
    • Figure 52 is a graph of an SEM/EPMA scan across the sample shown in Figure 51 and shows the fusion of cadmium with copper;
    • Figure 53 is a photomicrograph at x11,500 magnification of a steel matrix with which cadmium has been fused using the process of the present invention with a second cadmium solution;
    • Figure 54 is a graph of an SEM/EPMA scan across the sample shown in Figure 53 and shows the fusion of cadmium with steel;
    • Figure 55 is a composite photomicrograph with left and right hand halves, of a copper matrix with which tin has been fused using the process of the present invention with a first tin solution; the left hand half has a magnification of x655 and the right hand half is a x8 enlargement of the marked area;
    • Figure 56 is an SEM/EPMA scan across the sample of Figure 55 and shows the fusion of tin with copper;
    • Figure 57 is a composite photomicrograph with left and right hand halves, of a copper matrix with which tin has been fused using the process of the present invention with a second tin solution; the left hand half has a magnification x326 and the right hand half is x8 enlargement of the marked area;
    • Figure 58 is an SEM/EPMA scan across the sample of Figure 57 and shows fusion of tin with copper;
    • Figure 59 is a composite SEM photomicrograph with right and left hand halves, of a steel matrix with which tin has been fused using the process of the present invention with the second tin solution; the right hand half is a x1310 magnification and the left hand half is x8 magnification of the marked area;
    • Figure 60 is a SEM/EPMA scan across the sample of Figure 59 and shows fusion of tin with steel;
    • Figure 61 is an SEM photomicrograph at a x5200 magnification of a copper matrix with which cobalt has been fused using the process of the present invention with a first cobalt solution;
    • Figure 62 is an SEM/EPMA scan across the sample of Figure 61 and shows fusion of cobalt with copper;
    • Figures 63 and 63A are photomicrographs of a copper matrix with which silver has been fused using the process of the invention with a first silver solution;
    • Figure 63 is a composite with the left hand side having a magnification of x625 and the right hand side being an x8 enlargement of the marked area;
    • Figure 63A is a further enlarged SEM photomicrograph of the enlarged area of Figure 63 at a magnification x 10,000;
    • Figure 64 is an SEM/EPMA scan across the sample of Figure 63 and shows fusion of silver with copper;
    • Figure 65 is an SEM photomicrograph at a magnification of x10,000 of a copper matrix with which silver has been fused using the process of the present invention with a second silver solution;
    • Figure 66 is an electron microprobe scan across the sample of Figure 65 and shows fusion of silver with copper;
  • In those Figures which are graphs, of Figures 19 through 66, the vertical axis is logarithmic while the horizontal axis is linear. And in these graphs the surface layer has been taken as the point at which the concentration (wt%) of the matrix and the element which has been fused therewith are both at 50% as indicated by the projections.
  • Referring now to drawings Figures 1 and 2 these drawings illustrate in general perspective view apparatus in accordance with the invention which is employed to carry out the process of the invention.
  • In Figure 1, which exemplifies a solid-to-solid process the number 10 indicates a power supply and 11 an oscillator.
  • One side of the oscillator output is connected to an electrode 13 through a holder 12. Holder 12 is provided with a rotating chuck and has a trigger switch which controls the speed of rotation of the electrode 13. The speed of rotation is variable from 5,000 to 10,000 rpm.
  • The electrode 13 is composed of the material to be fused with the matrix. The matrix or substrate which is to be subjected to the process and which is to be treated is indicated at 14. The matrix is also connected to the other side of the oscillator output by a clamp 15 and line 16.
  • By these connections the electrode is positively charged and the matrix is negatively charged when the signal is applied.
  • In Figure 2 the corresponding components are correspondingly numbered. However, in this embodiment the process employed may be characterized as a liquid to solid process. In this apparatus the material to be fused is in the form of a solution and is held in a reservoir 17. Reservoir 17 is connected by a tube 18 to an electrode 19. Electrode 19 is a plate provided with an insulated handle 20 through which one side of oscillator 11 output is connected. This output is led into a main channel 21 in electrode 19. Channel 21 has a series of side channels 22 which open on to the undersurface of electrode 20. The flow from reservoir 17 is by gravity or by a pump and may be controlled by a valve such as 23 on the handle 20. For further control more even distribution of the solution, and to prevent the inclusion of foreign matter the surface of electrode 19 is preferably covered by a permable membrane such as cotton or nylon.
  • It has been found that to effect fusion that the application of 50,000 watts/sq. cm. or alternatively the application of current of the order of 10,000 amps/sq. cm. is necessary.
  • From a practical standpoint 10,000 amps/sq. cm. can not be applied constantly without damage to the matrix to be treated.
  • However, it has been found practical to apply a pulsing signal of 2.5 microseconds to 28.6 nanoseconds having a magnitude of 3 amps to the electrode and this causes fusion to occur over an area of approximately 0.3 sq. mm.
  • To effect fusion over an area with the apparatus shown in Figure 1 the electrode 13, matrix 14 and the oscillator output are connected as shown.
  • The operator passes the rotating electrode 13 in contact with the upper surface of the matrix over the matrix surface at a predetermined speed to apply the electrode material to the matrix and fuse it therewith.
  • It has also been found that the continuous application of an alternating signal generates considerable heat in the substrate or matrix and to overcome this heat build-up and avoid weldments the signal generated in the present apparatus is a half-wave signal which permits dissipation of the heat.
  • As will be apparent to those skilled in the art each material, both the matrix and the material to be applied have specific resistance characteristics. Thus with each change in either one or both of these- materials there is a change in the resistivity of the circuit.
  • In Figure 3,
    • R1=the resistance of the electrode,
    • R2=the resistance of the matrix, and
    • R3=the resistance of the circuit of 10 and 11.
  • Variations in R1 and R2 will lead to variations in the frequency of the signal generated and the amplitude of that signal.
  • As mentioned previously a signal having an amplitude of 3 amps is believed to be the preferred amplitude. If the amplitude is greater decarbonizing or burning of the matrix takes place and below this amplitude hydroxides are formed in the interface.
  • Figure 4 is a schematic diagram of an oscillator circuit used in apparatus in accordance with the present invention.
  • In that circuit a power supply 30 is connected across the input, and across the input a capacitor 31 is connected. One side of the capacitor 31 is connected through the LC circuit 32 which comprises a variable inductance coil 33 and capacitor 34 connected in parallel.
  • LC circuit 32 is connected to one side of a crystal oscillator circuit comprising crystal 35, inductance 36, NPN transistor 37 and the RC circuit comprised of variable resistance 38 and capacitance 39.
  • This oscillator circuit is connected to output 50 through, on one side capacitor 40, and on the other side diode 41, to produce a halfwave signal across output 50.
  • In the apparatus actually used the several components had the following characteristics:
    • 31=1.2 farad
    • 32=0.3 picrofarad
    • 33=0-25 millihenrys
    • 35=400-30 KHZ
    • 36=20 millihenrys
    • 37=NPN
    • 38=3.5 p farads
    • 39=0-500 ohms
    • 40=400 µ farads
    • 41=diode
  • To maintain the amplitude of the signal at 3 amps R1 resistance 38 is varied; to vary the frequency inductance 33 is varied.
  • If C=the capacitance of the circuit of Figure 3 and R1, R2 and R3 are the resistances previously characterized it is believed that the optimum frequency of the fusing signal Fo may be determined by the form
    Figure imgb0001
    where
    • L=R1 · R2 · R3 and
    • C=capcitance of the circuit L and C may be determined by any well-known method.
    • Fa depends on the .material being treated and the material being applied but it is in the range 400 Hz-35 MHz. The frequency, it is believed, will determine the speed of the process.
  • To fuse a predetermined area, the area is measured. Since each discharge will fuse approximately 0.3 sq. mm. then the travel speed may be determined by the following form:
    Figure imgb0002
    and
    • A=area to be covered in sq. mm.
    • F1 is the number of discharges per second.
  • As mentioned previously the resistances R1 and R2 may be measured by any known means.
  • However it has been discovered that the measurement of resistance in the liquid phase may not be stable. In this situation the resistance is measured in a standard fashion. Two electrodes, 1 cm. apart and 1 cm. sq. in area are placed in a bath of the liquid phase and the resistance was measured after a 20 second delay. After the variable parameters have been determined and the apparatus, matrix and probe have been connected as shown in Figures 1 and 3, the probe 13 is passed over the surface of the matrix in contact therewith at the predetermined speed.
  • The speed of rotation is also believed to affect the quality of the fusion with a rotation speed of 5,000 rpm the finish is an uneven 200 to 300 finish; with a speed of rotation of 10,000 rpm the finish is a substantially 15 p finish.
  • The apparatus of Figure 2 is operated in the same manner as the apparatus of Figure 1 and the process is essentially the same except for the use of a liquid with a solid electrode.
  • The process may be more clearly understood from the following specific examples.
  • In each of these examples the electrode was so connected as will be apparent from the description, so that when charged the electrode is positively charged and the matrix is negatively charged.
  • The solid to solid process is illustrated by Examples I, II, IIA, III, and IV.
  • Example I
  • Atlas A151 01 tool steel was connected to the apparatus of Figure 1 as the matrix 14 and the electrode 13 was titanium carbide as Kennametal K165.
  • The following were the characteristics and conditions of treatment:
    Figure imgb0003
  • The results of the treatment of the Atlas A151 01 tool steel with the titanium carbide are shown in the microphotographs and spectrometer scans of Figures 5 through 17.
  • The polished titanium carbide treated steel was examined by SEM/EPMA and appeared as shown in Figure 5. X-ray spectra were taken at each of the numbered locations indicated in Figure 1, and they are shown in the graphs which are Figures 9 through 16 and which correspond to locations 1 through 8, respectively.
  • Figures 9, 10 and 11 give spectra from the parent metal.
  • Figures 12 through 16 show the presence of a small titanium peak which does not change markedly in height as the zone was crossed.
  • As will be seen in Figure 6, the approximate width of the zone in which titanium was detected is about 50 m although this dimension varied along the specimen length.
  • An examination of the surface layer using a microprobe analyzer gave the Ti Ka X-ray shown in Figure 7 which shows the titanium level to be fairly constant to measured depth of about 40 pm from the surface.
  • The sample was then given a heavy nickel coating and repolished. As illustrated in Figure 5 the resulting scanning electron micrograph indicates a surface coating of about one half of one micron. Figure 17 is an X-ray spectrum of this layer.
  • A hardness survey was then conducted on the coated steel sample and the results were as indicated in Table I.
    Figure imgb0004
  • As will be apparent the hardness characteristics of the steel were considerably enhanced.
  • Example II
  • 1018 Steel was connected to the apparatus of Figure 1 as the matrix 14 and the electrode 13 was molybdenum, Type Mo 1. The steel was 12.7 mm widex6.35 mm thickx38.1 mm long, the molybdenum 25.4 mm longx4 mm diameter. The frequency applied was 43.31 KHz and the speed of electrode rotation approximately 12,000 rpm.
  • The surface of the steel was ground to a surface finish of 600 grit. The electrode tip was moved manually along the top surface of the steel sample in straight lines adjacent to each other. The process was repeated at 90° to cover the whole surface. Under the optical microscope at x40 magnification small beads of melted and resolidified material were revealed.
  • As will be seen from Figure 18 the fusion of molybdenum with steel is quite evident.
  • The results of an electron microprobe scan across the interface revealed molybdenum to be present to a depth of at least 15 pm as shown in the Table below and Figure 19.
    Figure imgb0005
  • Microhardness measurements were taken on the cross-section of the sample with the following results:
    Figure imgb0006
  • The average KHN of the untreated steel was 188. The hardness of the same steel after heating to 900°C and water quenching was 285 (KHN) at 200 gm.
  • Example IIA
  • The same matrix and electrode and procedure as in Example II were followed at a frequency of 30.60 3 KHz and the same speed of rotation.
  • Under the optical microscope small beads of melted and resolidified material were revealed.
  • As will be seen from Figure 18A the fusion of molybdenum with steel is quite evident.
  • The results of an electromicroprobe scan across the interface revealed molybdenum to be present to a depth of at least 50 pm as shown in Figure 19A in the following Table:
    Figure imgb0007
  • Knoop microhardness measurements were taken on the cross-section of the sample. The results were as follows:
    Figure imgb0008
  • The hardness values of Examples II and IIA which exceed KHN 285 result from the presence of molybdenum.
  • Example III
  • Steel of the specifications as in Examples II and IIA was connected to the apparatus of Figure 1 as the matrix 14 and the electrode 13 was tungsten carbide (Kennametal Grade No. 68). This electrode was 5 mm diameterx25.4 mm long.
  • The frequency applied was 26.20 KHz and the speed of electrode rotation was approximately 12,000 rpm.
  • The procedure followed was the same as in Examples II and IIA.
  • As shown in Figure 20 tungsten is shown to be fused with the steel matrix. The results of an electron microscope analysis across the sample indicate the presence of tungsten to a depth of at least 80 pm and are shown in Figure 21 and the following table:
    Figure imgb0009
  • Knoop microhardness measurements were taken on the cross-section of the sample. The results were as follows:
    Figure imgb0010
  • The hardness of the untreated sample is approximately 188 KHN and after heating to 900°C and quenching was 285 KHN.
  • It is quite evident from the foregoing that the treatment of the steel matrix quite clearly enhances the surface hardness and it is useful in those applications where surface hardness is an important requirement.
  • With respect to the fusion of a second conductive chemical element into the solid matrix of a first conductive chemical element, using a solution of the second conductive chemical, with respect to each solution, the process was carried out at the ambient temperature, 20°C, in the following manner.
  • The matrix 14 metal was connected into the circuit as previously described. The frequency was determined in accordance with the formula previously set forth and the solution in reservoir 17 applied by movement of the electrode over one surface of the first metal for varying periods of time as determined by Form II. To ensure uniform distribution of the second metal solution over the surface of the first metal the electrode was covered with cotton gauze or nylon. It will be apparent that other materials may be employed. This arrangement also served to limit contamination of the solution when graphite electrodes were employed. They had a tendency to release graphite particles in the course of movement.
  • The treated samples were then sawn to provide a cross-sectional sample, washed in cold water, subject totultrasonic cleaning, embedded in plastic and ground and polished to produce a flat surface and an even edge. With other samples with the softer metals where there was a tendency to lose the edge on grinding two cross-sections were secured with the treated surface in face to face abutting relationship, embedded as before and ground and polished.
  • Following embeddment the sample was etched using Nital for steel, the ferrous substrate, and Ammonium Hydrogen Peroxide on the copper, the non-ferrous substrate.
  • During the course of some applications it was found that adjustments were sometimes required in either the frequency, or speed of application. These were due to changes in the solution composition or variations in the matrix.
  • A semiquantitative electron probe microanalysis of fused interfaces were performed using an Energy Dispersive X-Ray Spectroscopy (EDX) and a Scanning Electron Microscope (SEM).
  • The surface of the embedding plastic was rendered conductive by evaporating on it approximately 20 pm layer of carbon in a vacuum evaporator. This procedure was used to prevent buildup of electrical charges on an otherwise nonconductive material and a consequent instability of the SEM image. Carbon, which does not produce a radiation detectable by the EDX, was used in preference of a more conventional metallic coating to avoid interference of such a coating with the elemental analysis.
  • Operating conditions of the SEM were chosen to minimize extraneous signals and the continuum radiation and to yield at the same time the best possible spatial resolution.
  • The conditions typically used for the elemental analyses by EDX were as follows:
    Figure imgb0011
  • Energy calibration was tested using AI kd emission at 1.486 keV and cu K at 8.040 keV.
  • A standardless semiquantitative analysis was adopted for determination of elemental concentration, using certified reference materials (NBS 478, 78% Cu-27% Zn and NBS 479a, Ni, 11 %, Cr 18%, Fe) to verify results. Multiple analysis of reference materials were in excellent agreement with certified values from NBS. Average precision of ±1% was achieved. A size of analysed volume was calculated from the following equation 1:
    Figure imgb0012
    where
    • R(x) is the mass range (th x-ray production volume)
    • p=Density of analysed material
    • Eo=The accelerating potential
    • Ec=A critical excitation energy.
  • The diameter of analysed volume was calculated for typical elements analysed and was found to be as follows:
    Figure imgb0013
  • For assessment of the diffusion depth a static beam was positioned across the interface at intervals greater than the above mentioned mass range. Ensuring thus the accuracy of the analysis.
  • The results of elemental concentration were given in weight percentage (Wt.%) for each of the measured points across the fusion interface.
  • In the various examples which will be described the second conductive chemical element, that is the element to be diffused into the matrix, is present in solution. In some solutions small quantities of metallic ions of a third metal are also provided. The presence of these metal ions is believed to be required as complex forming agents to facilitate fusion. Small quantities of organic catalysts such as gum acacia, hydroquinone, animal glue, pepsin, dextrin, licorice, or their equivalents may also be present.
  • Wetting agents such as sodium lauryl sulphate or its equivalent are usually provided.
  • Where required pH varying agents such as ammonium hydroxide or sulphuric acid are usually added to reach an operating pH.
  • Certain further solutions require second chemical conductive element complexing agents which preclude precipitation of the second element. These agents were by way of example citric acid, or sodium pyrophosphate, or ethyldiaminetetracetic acid or their equivalents.
  • A suitable buffer is also provided in certain solutions, where required.
  • The water is always demineralized.
  • And for certain applications where the appearance of the product requires an elegant appearance small quantities of brighteners such as formaldehyde, carbon disulphide, benzene, sulphonic acid or their equivalents may be employed.
  • . In these Examples, unless otherwise indicated the steel matrix was ASA 1018 and the copper was ASTM B-1333 Alloy 110.
  • Example IV
  • Atlas A151 1020 steel was connected in the apparatus of Figure 2 as the matrix 14 and a 10% solution of ammonium molybdate in water was placed in reservoir 17.
  • The following were the characteristics and conditions of treatment:
    Figure imgb0014
  • The sample of Example IV was subject to a thermal corrosion test. 25% sulphuric acid was applied to the surface for 20 minutes at 325°C without any surface penetration.
  • Example V
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0015
  • The solution had the following characteristics:
    Figure imgb0016
  • The Mo+6 concentration may be varied from 1.5% to 2.5% by weight; the pH from 7.2 to 8.2 and the resistivity from 17-25 ohms cm.
    Figure imgb0017
  • In the solutions set out in Examples V and VI the presence of the ferrous and ferric ions are believed to serve to reduce the Mo+6 valency state to a lower valency state.
  • While iron is apparently concurrently transferred as illustrated in Figure 23 the iron has apparently no material effect on the characteristics of the matrix or the molybdenum.
  • An examination of the sample with an optical microscope shows a continuous coating of molybdenum free from pitting and with a dark silver colour.
  • As shown in the table below and Figure 23 an SEM/EPMA scan across the interface between the matrix and the applied metal, molybdenum is seen to be fused to a depth of at least 4 pm with a surface deposit of approximately 1 µm.
    Figure imgb0018
  • Example VI
  • An aqueous solution of the same formulation as Example V was prepared and applied under the following conditions:
    Figure imgb0019
  • Examination under the optical microscope showed a continuous dark silver surface.
  • The photomicrograph Figure 24, shows the deposition of a substantially uniform layer of molybdenum 1 micron thick of uniform density.
  • As shown in Figure 25 an SEM/EPMA scan across the interface between the substrate and the applied metal shows molybdenum was present to a depth of at least 10 microns and a molybdenum gradient as set out below in Table.
    Figure imgb0020
  • Example VII
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0021
  • The solution had the following characteristics:
    Figure imgb0022
    The W+6 concentration may vary from 1.6% to 2.5%; the pH may vary from 7.5 to 8.5; and the resistivity may vary from 18 ohms cm to 24 ohms cm.
    Figure imgb0023
  • As shown by the photomicrographs Figures 26 and 27, the sample showed a uniform deposit of tungsten approximately 1 micron thick. An SEM/EPMA scan showed fusion of tungsten on copper to a depth of at least 5.0 microns, as can be seen in the Table below and Figure 28.
    Figure imgb0024
  • Example VIII
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0025
  • The solution had the following characteristics:
    Figure imgb0026
  • The concentration of tungsten may be varied from 1.6% to 2.5% by wt.; the pH from 7.5 to 8.5; and the conductivity from 18.8 ohms cm to 22.8 ohms cm.
    Figure imgb0027
  • An inspection of the sample by SEM/EPMA, Figure 29, showed a deposit of tungsten of approximately 0.5 pm and as evident from Figure 30 and the Table below tungsten was detected at a depth of at least 3 µm.
    Figure imgb0028
  • Example IX
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0029
  • The solution had the following characteristics:
    Figure imgb0030
    The Indium concentration may vary from 0.2% to 2.2%; the pH from 1.60 to 1.68; and the resistivity from 48.8 ohms cm to 54.8 ohms cm.
    Figure imgb0031
  • An examination of the sample under the optical microscope and the scanning electron microscope showed a continuous surface free from structural faults as shown in Figure 31.
  • As shown in the following Table and Figure 32 and an SEM/EPMA scan across the interface between the copper matrix and the indium layer showed a deposit of approximately 1 µm and fusion of indium to a depth of at least 4 pm.
    Figure imgb0032
  • Example X
  • The solution of Example IX was employed and applied to a steel matrix:
    Figure imgb0033
  • As shown in Figures 33 and 34 an even continuous layer of Indium approximately 1 µm thick was deposited on the surface of the matrix. An SEM/EPMA scan, Figure 34 across the interface and the Table below indicated fusion to a depth of at least 3 µm:
    Figure imgb0034
  • Figure 35 shows a solid deposit of nickel of uniform density approximately 1.5 pm thick. As shown in the following Table and Figure 36 an SEM/EPMA scan across the interface between the matrix and the nickel layer shows nickel to be fused to a depth of at least 4 µm.
    Figure imgb0035
  • Example XI
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0036
    The solution had the following characteristics:
    Figure imgb0037
    The nickel concentration may vary from 2% to 10%; pH from 3.10 to 3.50; and resistivity from 17 ohms cm to 26 ohms cm.
    Figure imgb0038
  • Example XII
  • The same solution as was formulated for Example XI was prepared and applied to a steel matrix:
    Figure imgb0039
  • As shown in Figure 37 the nickel layer is continuous and substantially uniform in thickness being about 1.5 µm thick.
  • As shown in Figure 38 and in the following Table nickel is shown to be fused to a depth of at least 3 µm.
    Figure imgb0040
  • Example XIII
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0041
    This solution had the following characteristics:
    Figure imgb0042
    The pH may be varied from 3.70 to 11; the concentration of Au+3 ions may vary from 0.1% to 0.5% by weight; and the resistivity from 40 ohms cm to 72 ohms cm.
    Figure imgb0043
    Observation with the optical and scanning electron microscope revealed a surface deposition of gold approximately 1.5 µm thick. The deposit was continuous and uniformly dense as shown in Figure 39.
  • An SEM/EPMA scan across the interface indicated fusion of gold to a depth of at least 3 µm as shown on the Table below and Figure 40.
    Figure imgb0044
  • Example XIV
  • An aqueous solution of the same formulation as that of Example XIII was prepared:
    Figure imgb0045
    Observation with the optical and scanning electron microscope revealed a surface deposition of gold approximately 1.0 µm thick. The deposit was uniformly thick and dense as shown in Figure 41.
  • An SEM/EPMA scan across the interface indicated fusion of gold to a depth of at least 4.0 µm as shown on the table below and Figure 42.
    Figure imgb0046
  • Example XV
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0047
  • This solution had the following characteristics:
    Figure imgb0048
  • The pH may be varied from 0.6 to 1.0: the concentration of Cr+6 ions may vary from 3% to 20% by weight; and the resistivity from 11 ohms cm to 14 ohms cm.
    Figure imgb0049
    Observation with the optical and scanning electron microscope revealed a surface deposition of chromium approximately 1 pm thick. The surface of the layer was irregular but the deposit appeared free of faults and was continuous as shown in Figure 43.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 3.0 µm as shown on the table below and Figure 44.
    Figure imgb0050
  • Example XVI
  • An aqueous solution of the same formulation as employed in Example XV was prepared:
    Figure imgb0051
    Observation with the optical and scanning electrode microscope revealed a surface deposition of chromium approximately 3.0 µm thick. This is as shown in Figure 45.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 5.0 µm as shown on the Table below and Figure 46.
    Figure imgb0052
  • Example XVII
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0053
    This solution had the following characteristics:
    Figure imgb0054
    The pH may be varied from 2.5 to 3.5; the concentration of Cr+3 ions may vary from 1.8% to 5% by weight; and the resistivity from 16 ohms cm to 20 ohms cm.
    Figure imgb0055
    Observation with the optical and scanning electron microscope revealed a surface deposition of chromium approximately 0.5 µm thick. The deposit was solid and continuous as shown in Figures 47 and 47A.
  • An SEM/EPMA scan across the interface indicated fusion of chromium ta a depth of at least 3.0 µm as shown on the Table below and Figure 48.
    Figure imgb0056
  • Example XVIII
  • An aqueous solution of the same formulation as prepared for Example XVII was employed:
    Figure imgb0057
    Observation with the optical and scanning electron microscope revealed a surface deposition of chromium approximately 1.0 pm thick. The surface of the deposit appeared slightly irregular but the deposit was solid and free of faults as shown in Figures 49 and 49A.
  • An SEM/EPMA scan across the interface indicated fusion of chromium to a depth of at least 3.0 µm as shown on the Table below and Figure 50.
    Figure imgb0058
  • Example XIX
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0059
  • This solution had the following characteristics:
    Figure imgb0060
  • The pH may be varied from 10 to 10.2; the concentration of Cd+2 ions may vary from 0.2% to 0.5% by weight; and the resistivity from 28 ohms cm to 35 ohms cm.
    Figure imgb0061
    In this Example the solution employed was initially as set out above, applied in accordance with the conditions identified as (1). A second solution, that set forth in Example XX, was then applied under the conditions identified as (2). Observation with the optical and scanning electron microscope revealed a surface deposition of cadmium approximately 4 pm thick. This deposit was not homogeneous as shown in Figure 51 but an SEM/EPMA scan across the interface indicated fusion of cadmium to a depth of at least 9 µm as shown on the Table below and Figure 52.
    Figure imgb0062
  • Example XX
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0063
  • This solution had the following characteristics:
    Figure imgb0064
    The pH may be varied from 3.2 to 3.5; the concentration of Cd+2 ions may vary from 1 % to 4% by weight; and the resistivity from 45 ohms cm to 55 ohms cm.
    Figure imgb0065
    Observation with the optical and scanning electron microscope revealed a surface deposition of cadmium approximately 1 pm thick. The surface of the deposit was irregular but it was solid and continuous as seen from Figure 53.
  • An SEM/EPMA scan across the interface indicated fusion of cadmium to a depth of at least 4 pm as shown on the Table below and Figure 54.
    Figure imgb0066
  • Example XXI
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0067
  • This solution had the following characteristics:
    Figure imgb0068
    The pH may be varied from 11.2 to 12.7; the concentration of Sn+2 ions may vary from 2% to 5% by weight; and the resistivity from 6.2 ohms cm to 10.3 ohms cm.
    Figure imgb0069
    Observation with the optical and scanning electron microscope revealed a surface deposition of tin approximately 1.2 µm thick. The deposit was uniformly thick and homogeneous. This is shown in Figure 55.
  • An SEM/EPMA scan across the interface indicated fusion of tin to a depth of at least 4 µm as shown on the table below and Figure 56.
    Figure imgb0070
  • Example XXII
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0071
  • This solution had the following characteristics:
    Figure imgb0072
    The pH may be varied from 9 to 9.7; the concentration of Sn+2 ions may vary from 0.4% to 1% by weight; and the resistivity from 30 ohms cm to 36 ohms cm.
    Figure imgb0073
    Observation with the optical and scanning electron microscope revealed a surface deposition of tin approximately 4 pm thick. This deposit appears to comprise a lower uniform and substantially homogenous layer of approximately 1 µm thick and an outer slightly porous layer approximately 3 µm thick as shown in Figure 57.
  • An SEM/EPMA scan across the interface indicated fusion of tin to a depth of at least 5 µm as shown on the Table below and Figure 58.
    Figure imgb0074
  • Example XXIII -
  • An aqueous solution of the same as prepared for Example XXII was employed:
    Figure imgb0075
    Observation with the optical and scanning electron microscope revealed a surface deposition of tin exceeding 2 µm thick. This layer was porous but continuous as shown in Figure 59.
  • An SEM/EPMA scan across the interface indicated fusion of tin to a depth of at least 2 pm as shown on the Table below and Figure 60.
    Figure imgb0076
  • Example XXIV
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0077
  • This solution had the following characteristics:
    Figure imgb0078
    The pH may be varied from 4.5 to 6.5 the concentration of Co+2 ions may vary from 2% to 6% by weight; and the resistivity from 25 ohms cm to 30 ohms cm.
    Figure imgb0079
    Observation with the optical and scanning electron microscope revealed a surface deposition of cobalt approximately 6.5 pm thick. This layer was uniform and continuous as shown in Figure 61.
  • An SEM/EPMA scan across the interface indicated fusion of cobalt to a depth of at least 20 um as shown on the Table below and Fig. 62.
    Figure imgb0080
  • It was evident by visual inspection and from the previous experiments that the deposit of cobalt was above the 10 µm level was extremely dense.
  • Example XXV
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0081
  • This solution had the following characteristics:
    Figure imgb0082
    The pH may be varied from 11.2 to 11.7; the concentration of Ag+1 ions may vary from 1% to 3% by weight; and the resistivity from 8 ohms cm to 13 ohms cm.
    Figure imgb0083
    Observation with the optical and scanning electron microscope revealed a surface deposition of silver approximately 5 µm thick. The structure is shown in Figures 63 and 63A.
  • An SEM/EPMA scan across the interface indicated fusion of silver to a depth of at least 3 µm as shown on the Table below and Figure 64.
    Figure imgb0084
  • Example XXVI
  • An aqueous solution of the following formulation was prepared:
    Figure imgb0085
  • This solution had the following characteristics:
    Figure imgb0086
    The pH may be varied from 1.5 to 2; the concentration of Ag+1 ions may vary from 0.5% to 2.5% by weight; and the resistivity from 6 ohms cm to 12 ohms cm.
    Figure imgb0087
    Observation with the optical and scanning electron microscope revealed a surface deposition of silver approximately 2 pm thick. The structure was as shown in Figure 65.
  • An SEM/EPMA scan across the interface indicated fusion of silver to a depth of at least 2.00 J.lm as shown on the Table below and Figure 66.
    Figure imgb0088
  • From the foregoing Examples it will be seen that the present application discloses a novel process, apparatus for carrying out the process, solutions for use in the process, and new products which are capable of a wide variety of applications and uses.
  • It is also to be noted that while the description has been with respect to Examples in which the application was across the entire surfaces it is quite evident that the application may be limited to specific areas of surfaces depending to give a specific desired result.
  • For example tin, gold and silver, with their inherent excellent conductivity characteristics may be employed in electrical applications and circuits may be fused on other substrates.
  • The anti-corrosion characteristics of tin, gold, silver, nickel, chromium, cadmium, molybdenum and tungsten are also useful. And the application of those metals to ferrous or non-ferrous substrates will enhance their anti-corrosion behavior.
  • Chromium, nickel, silver, gold or tin have the capability of imparting an elegant appearance to the matrix. Chromium, molybdenum, tungsten, titanium and cobalt impart a surface hardness to the matrix.
  • Indium imparts strength to the matrix, and also serves as anti-galling agent. A molybdenum treated ferrous or non-ferrous matrix has improved friction-wear and high temperature resistance characteristics. It is also useful as a dielectric coating.
  • A cadmium fused matrix as well as having enhanced corrosion resistance characteristics can also serve as an anti-fouling agent for ship hull treatment.
  • Silver fused matrices are all useful as a reflecting medium.
  • It will be apparent that the process and apparatus are extremely facile to use without large capital expenditure and plant and permit the use of materials in applications which were not heretofore contemplated at less expense than previously and apart from the applications and uses specified many others will be apparent to those skilled in the art.
  • It will also be apparent that the various parameters in the process may be varied depending on the variables which may be encountered and the results required without departing from the spirit and scope of the invention as defined in the claims annexed.

Claims (6)

1. Process for the fusion, at an ambient temperature, of at least one second conductive element comprising ferrous or non-ferrous metals or alloys thereof into a matrix of a first conductive element comprising a ferrous or non-ferrous metals or alloys thereof, said process comprising the steps of
(a) bringing said conductive element into contact with a limited area of an adjacent surface of said first conductive element,
(b) applying a half-wave interrupted pulsing signal in the range of 2.5 microseconds to 28.6 nanoseconds with a frequency of 400 Hz to 35 MHz and an amplitude of about 3 amps over an area of about 0.3 square mm, and
(c) fusing said conductive element in said first conductive element to a depth of more than 0.5 J.lm and depositing a surface layer of said second chemical element of more than 0.5 pm thickness.
2. A process as claimed in Claim 1 whereby said second conductive element is in the form of a solid electrode including said second conductive element.
3. A process as claimed in any one of Claims 1 to 2 characterized in that said first conductive element is chosen from the group comprising ferrous metals or an alloy thereof and said second conductive element is chosen from the group comprising non-ferrous metals or an alloy thereof.
4. A process as claimed in any one of Claims 1 to 2 characterized in that said first conductive element is chosen from the group comprising non-ferrous metals or an alloy thereof and said second conductive element is chosen from the group comprising ferrous metals or alloys thereof.
5. Process according to any of Claims 1-4 wherein the second conductive element is rotated at a speed in the range from about 5,000 to about 10,000 rpm.
6. Process according to any of Claims 1, to 5 characterized in that the second conductive element is in liquid form.
EP82300138A 1981-01-13 1982-01-12 Process and apparatus for treating electrically conductive matrices and products produced by the process Expired EP0056331B1 (en)

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US4206028A (en) * 1976-12-14 1980-06-03 Inoue-Japax Research Incorporated Electrochemical polishing system
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