Patent Application
20110073486
The invention relates generally to amorphous metallic materials, and particularly to methods for altering a dimension of amorphous metallic materials.
Generally, amorphous metallic materials exhibit high permeability and ease of magnetization. Typically, cores for electric devices such as transformers, inductors or motors are formed by amorphous metallic materials that are arranged to form a stack or a coil. These stacks or coils are then cut into desired shapes to be employed in the core.
Conventional amorphous metallic materials are formed by rapid solidification of an alloy, that is, by cooling the alloy to a temperature below the glass transition temperature before appreciable nucleation and crystallization has occurred. Melt spinning is typically employed to fabricate metallic glass ribbons or tapes that have some flexibility.
Amorphous metallic materials generally are prepared with small dimensions due to the need to extract heat during solidification at a sufficient rate to suppress crystallization. However, the currently employed processes, such as melt spinning, often are subject to process limitations that prevent producing articles with desired dimensions. For example, amorphous metallic material ribbons produced by employing melt spinning have thickness values higher than desired for certain high frequency applications. Amorphous metallic material ribbons with reduced thicknesses are useful for achieving lower core loss properties due to a reduction in the eddy current losses which are proportional to the amorphous metallic material ribbon cross-sectional area.
Therefore, there is a need for providing a method for altering a dimension of an element made of amorphous metallic materials.
One embodiment of the present invention provides a method for altering a dimension of an element made of an amorphous metallic material. The method includes providing an anode comprising the amorphous metallic material, wherein the amorphous metallic material comprises at least two primary constituents, providing a cathode disposed in a spaced-apart relationship with the anode, providing an electrolyte in contact with the anode and the cathode, and applying an electrical potential between the anode and the cathode.
Another embodiment of the present invention provides a method for altering a dimension of an element made of an amorphous metallic material. The method includes providing an anode feedstock comprising the amorphous metallic material, wherein the amorphous metallic material comprises at least two primary constituents, providing a cathode; providing an electrolyte in contact with a portion of the anode feedstock and the cathode, wherein the portion of the anode feedstock and the cathode are disposed in a spaced-apart relationship, applying an electrical potential between cathode and the portion of the anode feedstock that is disposed in the electrolyte, and continuously feeding the anode feedstock into the electrolyte.
Yet another embodiment of the present invention provides a method for uniformly reducing a thickness of a metallic glass ribbon. The method includes providing the metallic glass ribbon as an anode feedstock, disposing the metallic glass ribbon in an electrolyte bath, wherein the electrolyte bath comprises phosphoric acid; providing a cathode in a spaced-apart relationship with the metallic glass ribbon, and applying an electrical potential between the metallic glass ribbon and the cathode to remove at least a part of the two primary constituents from the metallic glass ribbon.
These and other features, aspects, and advantages of the present invention will become better understood when the following detailed description is read with reference to the accompanying drawings in which like characters represent like parts throughout the drawings, wherein:
Embodiments of the present invention include methods for altering a dimension of an element made of an amorphous metallic material. As used herein, the term “amorphous metallic material” refers to a magnetic material where a continuous matrix phase has an amorphous nature, i.e. a disordered atomic-scale structure that does not have long-range crystallographic order. The amorphous metallic material may also include crystalline phases within the amorphous matrix. In certain embodiments, the amorphous metallic material is a metallic glass ribbon that exhibits soft magnetic properties. The method is based on the principle of electrochemical machining (ECM). ECM uses electrical potential energy to drive chemical reactions that remove material from a workpiece (anode). Typically in ECM, an electrolytic cell is created in an electrolyte medium, with a cathode (tool) and an anode (workpiece).
Generally, amorphous metallic materials are not easy to machine or work into desired shapes. Conventional machining may induce defects or stresses that degrade the magnetic properties of the material. For this reason, the methods of fabricating these materials, such as melt spinning, for example, are often relied upon to produce the articles of desired shapes, with little or no mechanical post-processing. However, due to process limitations, it may not be often feasible to produce directly the element with desired shape and dimensions.
Conventionally, the ECM process is employed to form intricate parts from otherwise strong, generally crystalline, metals. However, the application of ECM to amorphous metallic materials requires special considerations to achieve proper results. In embodiments of the present invention, employing the ECM process includes carefully selecting an electrolyte that ensures none or very limited structural damage to the anode. The electrolyte is selected such that the component materials of the anode have substantially similar removal rates in the presence of the selected electrolyte solution, to avoid deleterious alteration of the anode composition and properties. In certain embodiments, the method enables the amorphous metallic material to retain its magnetic properties while altering the material shape and dimensions.
In certain embodiments, the method includes providing an anode, which comprises the amorphous metallic material. The amorphous metallic material of the anode includes at least two primary constituents. The two primary constituents are capable of being oxidized during the process. A cathode is disposed in a spaced-apart relationship with the anode. Both the anode and cathode are in contact with an electrolyte. An electrical potential is applied for a period of time between the anode and the cathode via the electrolyte. In certain embodiments, a high-amperage, low-voltage current is employed to dissolve the two primary constituents from the anode into the electrolyte. In one embodiment, the current may be a pulsed current. Upon application of the voltage, at least a portion of the two primary constituents in the anode are oxidized. The constituents that are oxidized are primarily from the surface of the anode; the oxidized constituents (metal ions) may form hydroxides that are dissolved or otherwise entrained in the electrolyte.
The metal hydroxides in the electrolyte form undesired/unwanted sludge in the electrolyte. In certain embodiments, the sludge containing the hydroxides may be removed from the electrolyte by centrifugal separation. Both the electrolyte and the sludge may be recycled and regenerated. Regeneration of the electrolyte is particularly useful when employing a continuous process. Non-limiting examples of regeneration of the electrolyte may include filtration, reverse plating, and chemical monitoring where “make-up” fresh electrolyte is used to keep electrolyte conductivity within certain process boundaries. In certain embodiments, filtration and periodic addition of fresh solution are used for regeneration of the electrolyte. Filtration may use a porous media. In one example, the filter may be a bag or a tube that retains and removes the precipitated hydroxides. In one embodiment, the anode and the cathode may be disposed in a flowing electrolyte solution, such that the flowing electrolyte solution washes the metal ions away from the anode. The flowing electrolyte solution may be periodically recycled and regenerated.
In some embodiments, the methods of the present invention may be employed to uniformly reduce a thickness of the anode. As used herein, the term “uniformly” means that the reduction in thickness at any given portion is within 5 percent deviation throughout the surface of the element that is undergoing reduction in thickness. In these embodiments, the distance between anode and cathode is substantially the same throughout the body of the anode and cathode. In one example, the thickness of the anode may be reduced from about 30 microns to about 10 microns.
In other embodiments, a dimension of the element may be altered non-uniformly. For example, the intentional non-uniform reduction in thickness may be to provide a desired shape to at least a portion of the anode. In these embodiments, the distance between the anode and cathode may be varied for different portions of the anode and cathode. Because of the electrical resistance of the electrolyte, for a given electrode geometry the current density is typically the highest at the position where the distance between the anode and cathode is the smallest. As a result the corresponding area of the anode closest to the cathode may dissolve at the highest rate. That is, the different distances result in different removal rates of the material from the anode, thereby resulting in different amounts of reduction in thickness at the different portions of the anode. Accordingly, different shapes, contours, angles, edges, cavities, and the like may be formed in the element by employing the present technique.
As illustrated in the flow chart of
At block 14, a cathode is disposed in a spaced-apart relationship with the anode. Non-limiting examples of the cathode material may include copper, copper-tungsten, brass, stainless steel, titanium, gold, platinum, graphite and the like. The distance between the cathode and anode is relatively small. Initially, the distance between the cathode and the anode may be just a few millimeters. For example, the distance between the cathode and the anode before the commencement of the process may be in a range from about 1 millimeter to about 3 millimeters.
In one embodiment, the space between the cathode and the anode may be kept substantially constant during the process. As used herein, the term “substantially constant” is defined as falling within industry recognized manufacturing tolerances, and ordinary and anticipated dimensional variations in the process and may encompass variations in a range from about −5 percent to about +5 percent. In this embodiment, the anode or the cathode may be moved with respect to each other to maintain the constant distance as the dimension of the anode is altered during the process. For example, the cathode may be gradually moved towards the anode as the thickness of the anode is gradually reduced during the process. The speed with which the anode or the cathode is moved may depend on the rate of removal of the material from the surface of the anode. In one example, as the machining proceeds, the simultaneous movement of the cathode may be set at about 0.02 millimeter/second toward the anode. In one embodiment, the distance between the anode and cathode may be maintained at about 0.4 millimeters throughout the process.
In another embodiment, the distance between the cathode and the anode may vary during the process. For example, if the position of the cathode and the anode is fixed, the alteration in the dimension of the element may result in the increase in space between the anode and the cathode. In one example, the distance between the anode and the cathode may increase with the reduction in thickness of the anode. In one embodiment, the distance between the anode and the cathode before the commencement of the process is in a range from about 1 millimeter to about 1.5 millimeters.
At block 16, an electrolyte is provided in contact with the anode and the cathode. Typically, neutral salts are preferred as electrolytes for conventional ECM process. However, in embodiments of the present invention, an aqueous-based acidic electrolyte is employed to dissolve the at least two primary constituents from the anode. In certain embodiments, a pH of the electrolyte is in a range from about 2 to about 6, in particular embodiments; the pH is in a range from about 2 to about 4. In one embodiment, the electrolyte may be an aqueous solution of phosphoric acid. In one example, the electrolyte comprises about 70 percent by weight to about 90 percent by weight phosphoric acid in an aqueous solution.
The electrolyte is selected such that the electrolyte achieves acceptable levels of anode material removal without undue damage to cathode materials. An electrolyte having a high amount of phosphoric acid (for example, 85 percent by weight and higher) is required to be handled safely due to the toxicity of such an electrolyte. Also, the electrolyte is desirably able to maintain certain significant characteristics, such as its composition and pH value, during the machining period. The electrolyte has substantially similar material removal rates for the primary constituents of the amorphous metallic material. In addition to the electrolyte composition, the rate of removal of the at least two primary constituents may depend on the atomic weight and the ionic charge of the two primary constituents, the amount of current which is passed through the anode, and the time for which the current passes. The substantially similar material removal rates for the two primary constituents facilitate alteration of the dimension of the anode while preventing formation of pin holes, or any such structural defects in the anode; in addition, the similar removal rate provides for material removal without substantially altering the composition and properties of the remaining anode material.
The anions in the electrolyte are typically selected to avoid or minimize passive film formation on the surface of the anode during the dissolution process. However, it should be noted that obtaining a product having a very thin oxide layer may be desirable for certain applications. In such cases, process conditions may be manipulated to leave a passive oxide layer on the surface of the anode at the end of the process. In addition, the cations in the electrolyte should not deposit on the cathode surface so that the cathode shape remains unchanged.
In one embodiment, the electrolyte may have a forward flow, a reverse flow, or a side flow. Forward flow has the electrode and electrolyte moving in the same direction. Reverse flow has the electrode and electrolyte moving in opposite directions. The reverse flow can be counter current. Side flow has the electrolyte flowing perpendicular to the direction of electrode movement. The selection of the flow method may be based on the shape of the anode. Typically, forward and reverse flows are employed to drill holes or forming cavities, whereas the side flow method is often used for non-cavity shaping, such as profile formation, thickness reduction. It is desirable to have the electrolyte flow uniformly over the entire surface of the anode undergoing alteration in dimension.
In certain embodiments, the electrolyte is pumped through the interelectrode gap so that the products of the electrolysis are carried away. The forced movement of the electrolyte also diminishes the effects both of electrical heating of the electrolyte (resulting from the passage of current) and formation of hydrogen gas; these two effects respectively increase and decrease the effective conductivity of the electrolyte. The electrolyte carries away heat generated by the process, thus maintaining a constant temperature in the region in and around the electrodes. Moreover, the flow of the electrolyte enables removal of the debris of the electrochemical reactions from the gap between the anode and the cathode.
At block 18, an electrical potential is applied for a period of time between the anode and the cathode. The electrical potential drives the electrochemical reaction between the anode and the cathode as a result of which at least two primary constituents of the anode are oxidized at the anode and dissolve in the electrolyte solution. The dissolution of the two primary constituents in the electrolyte results in alteration of the dimension of the anode. For example, the dissolution of the two primary constituents in the electrolyte results in reduction in thickness of the anode. In one embodiment, the potential applied may be in a range from about 2 volts to about 5 volts. The period of time for applying the potential may depend upon the amount of alteration in the dimension desirable at the anode. The period of time may be in a range from about 2 minutes to about 60 minutes. In one embodiment, the period of time may be about 30 minutes. The value of the applied potential may depend on the chemical composition of the anode. For example, for a chemical composition in weight percent of Fe 62.4 percent, Co 15.6 percent, Mo 1 percent, P 10 percent, B 3 percent, C 7 percent, and Si 1 percent, the applied potential is about 4 volts.
The electrical current for the process may be in a range from about 50 mA to about 10 A. Generally, under processing conditions where current is attributable mostly to the dissolution of material, a higher current density results in a faster material removal rate. The current may be a DC current. The current may be a pulsed current. In one example, periodic application and removal of potential may provide a short pulse of anode dissolution. The short pulse of anode dissolution may be followed by a short interval where no reaction is occurring prior to the next pulse of anode dissolution.
The metallic glass ribbon 22 may run in the electrolyte bath 24 at a constant speed. The speed of the metallic glass ribbon 22 is such that a given portion of the metallic glass ribbon 22 is placed in the electrolyte bath 24 for a determined period of time to enable a required amount of dissolution of the material from the anode in the electrolyte bath 24.
A cathode (not shown) is disposed at the bottom (not shown) of the electrolyte bath 24. The cathode may run along the length of the electrolyte bath 24 and be in the form of a strip that may cover at least a portion of the bottom across the width of the electrolyte bath 24.
Optionally, after passing through the electrolyte bath 24, the metallic glass ribbon 22 may be rinsed in a de-ionized (DI) water bath 34. In the illustrated embodiment, the DI water bath 34 is disposed adjacent to the electrolyte bath 24. A spool 36 is employed to transfer the metallic glass ribbon 22 from the electrolyte bath 24 to the DI water bath 34. In the DI water bath 34, the metallic glass ribbon runs on the spools 38 and 40. The DI water may be periodically replaced or replenished.
In addition, a filter may be in operative association with the electrolyte bath 24, such that the electrolyte bath 24 may be periodically filtered to remove at least a part of the sludge. The filtered electrolyte may be pumped back in the electrolyte bath 24 by employing a pump. The electrolyte may also be subjected to precipitation prior to being filtered. The precipitation may be carried out to reduce the amount of sludge from the electrolyte by precipitating the metal hydroxides. An electrolyte reservoir may be coupled to the system to pump in fresh (non-contaminated) electrolyte periodically.
Although not illustrated, in a simpler arrangement requiring more space, the DI water bath 34 may be in a straight-line configuration with the electrolyte bath 24.
In certain embodiments, the amorphous metallic material element processed in accordance with the above method is employed in an electrical device such as a core used in a transformer, inductor or motor. To obtain optimum magnetic properties in magnetic cores made from metallic glass ribbons, toroidal cores are first wound in their final configuration and then annealed, often with a magnetic field applied.
Other applications for the amorphous metallic material element of the present technique may include power transformers, common mode chokes, magnetic amplifiers, high precision current transformers for electronic energy meters, ISDN-transformer, sensors, such as fluxgate magnetometer, stress sensor, security sensor.
The effects of four different electrolyte compositions were studied for dissolution of a metallic glass ribbon. The nominal chemical composition of the metallic glass ribbon in weight percent was Fe 62.4 percent, Co 15.6 percent, Mo 1 percent, P 10 percent, B 3 percent, C 7 percent, and Si 1 percent. The metallic glass ribbon was fabricated using melt spinning equipment. The thickness of the ribbon was about 23 microns.
The ribbon was cut into four pieces and, after being rinsed with deionized water, each piece was separately immersed in four different types of electrolyte baths. The cathode was made of oxygen free copper. The cathode was approximately 5 times larger in area than the area of ribbon exposed in the electrolyte solution. The first electrolyte bath was a 10 percent aqueous solution of sodium nitrate. The second electrolyte bath was 1 M sulfuric acid. The third electrolyte bath was a mixture of hydrofluoric, nitric, and hydrochloric acids. The fourth electrolyte bath was an aqueous solution of 85 weight percent phosphoric acid. The ribbons were immersed for a period of 10 minutes. An electric potential of 4 volts was applied across the electrolyte baths.
The ribbons in the first, second and third electrolyte baths were oxidized on the surface or throughout the entire cross-section. This oxidation was undesirable for usage as magnetic cores. The ribbon in the fourth electrolyte bath using aqueous solution of phophoric acid did not result in any surface oxide, and provided a good surface finish, by substantially avoiding formation of pin holes, and a uniformly reduced thickness of about 10 microns.
Commercially available metallic glass ribbons from Hitachi including METGLAS 2605SC, METGLAS 2605S-3A, METGLAS 2705M, METGLAS 2826MB, and METGLAS 2605CO were subjected to 85 percent phosphoric acid solution. Each ribbon sample was subjected to 4 volts applied potential for 10 minutes. All the samples were successfully thinned using the method of the present application. The samples did not display any adverse effects with respect to the magnetic properties.
While only certain features of the invention have been illustrated and described herein, many modifications and changes will occur to those skilled in the art. It is, therefore, to be understood that the appended claims are intended to cover all such modifications and changes as fall within the true spirit of the invention.
This invention was made with Government support under contract number N00014-07-C-0550 awarded by U.S. Office of Naval Research. The Government has certain rights in the invention.
